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Annex 2
WHO good manufacturing practices: water for
pharmaceutical use
1
1. Introduction 68
1.1 Scope of the document 68
1.2 Background to water requirements and uses 68
1.3 Applicable guides 69
2. General principles for pharmaceutical water systems 69
3. Water quality specifications 70
3.1 General 70
3.2 Drinking-water 70
3.3 Bulk purified water 71
3.4 Bulk highly purified water 71
3.5 Bulk water for injections 72
3.6 Other grades of water 72
4. Application of specific types of water to processes and dosage forms 72
5. Water purification systems 73
5.1 General considerations 73
5.2 Production of drinking-water 74
5.3 Production of purified water 76
5.4 Production of highly purified water 77
5.5 Production of water for injection(s) 77
6. Water storage and distribution systems 78
6.1 General 78
6.2 Materials that come into contact with systems for water for pharmaceutical use 78
6.3 System sanitization and bioburden control 80
6.4 Storage vessel requirements 80
6.5 Requirements for water distribution pipework 81
7. Operational considerations 83
7.1 Start-up and commissioning of water systems 83
7.2 Qualification 83
7.3 Continuous system monitoring 85
7.4 Maintenance of water systems 86
7.5 System reviews 86
8. Inspection of water systems 87
Further reading 88
1 The current document is a revision of WHO good manufacturing practices: water for pharmaceutical use,
previously published in WHO Technical Report Series, No. 929, Annex 3, 2005.
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1. Introduction
1.1 Scope of the document
1.1.1 e guidance contained in this document is intended to provide information
about the available specications for water for pharmaceutical use (WPU),
guidance about which quality of water to use for specic applications, such as
the manufacture of active pharmaceutical ingredients (APIs) and dosage forms,
and to provide guidance on good manufacturing practices (GMP) regarding the
design, installation and operation of pharmaceutical water systems. Although the
focus of this document is on water for pharmaceutical applications, the guidelines
may also be relevant to other industrial or specic uses where the specications
and practices can be applied.
Note: is document does not cover water for administration to patients
in the formulated state or the use of small quantities of water in pharmacies to
compound individually prescribed medicines.
1.1.2 e GMP guidance for WPU contained in this document is intended to
be supplementary to the general GMP guidelines for pharmaceutical products
published by WHO (WHO Expert Committee on Specications for Pharmaceutical
Preparations. irty-seventh report. Geneva, World Health Organization, 2003
(WHO Technical Report Series, No. 908), Annex 4).
1.1.3 is document refers to available specications, such as the pharmaco-
poeias and industry guidance for the use, production, storage and distribution of
water in bulk form. In order to avoid confusion it does not attempt to duplicate
such material.
1.1.4 e guidance provided in this document can be used in whole or in part
as appropriate to the application under consideration.
1.1.5 Where subtle points of dierence exist between pharmacopoeial speci-
cations, the manufacturer will be expected to decide which option to choose in
accordance with the related marketing authorization submitted to the national
medicines regulatory authority.
1.2 Background to water requirements and uses
1.2.1 Water is the most widely used substance, raw material or starting material
in the production, processing and formulation of pharmaceutical products.
It has unique chemical properties due to its polarity and hydrogen bonds.
This means it is able to dissolve, absorb, adsorb or suspend many different
compounds. These include contaminants that may represent hazards in
themselves or that may be able to react with intended product substances,
resulting in hazards to health.
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1.2.2 Control of the quality of water throughout the production, storage and dis-
tribution processes, including microbiological and chemical quality, is a major con-
cern. Unlike other product and process ingredients, water is usually drawn from a
system on demand, and is not subject to testing and batch or lot release before use.
Assurance of quality to meet the on-demand expectation is, therefore, essential.
Additionally, certain microbiological tests may require periods of incubation and,
therefore, the results are likely to lag behind the water use.
1.2.3 Control of the microbiological quality of WPU is a high priority. Some
types of microorganism may proliferate in water treatment components and in
the storage and distribution systems. It is crucial to minimize microbial contami-
nation by proper design of the system, periodic sanitization and by taking appro-
priate measures to prevent microbial proliferation.
1.2.4 Dierent grades of water quality are required depending on the route
of administration of the pharmaceutical products. Other sources of guidance
about dierent grades of water can be found in pharmacopoeias and related
documents.
1.3 Applicable guides
1.3.1 In addition to the specic guidance provided in this document, the Further
reading section includes some relevant publications that can serve as additional
background material when planning, installing and using systems intended to
provide WPU.
2. General principles for pharmaceutical water systems
2.1 Pharmaceutical water production, storage and distribution systems should be
designed, installed, commissioned, qualied and maintained to ensure the reliable
production of water of an appropriate quality. It is necessary to validate the water
production process to ensure the water generated, stored and distributed is not
beyond the designed capacity and meets its specications.
2.2 The capacity of the system should be designed to meet the average and the
peak ow demand of the current operation. If necessary, depending on planned
future demands, the system should be designed to permit increases in the capac-
ity or designed to permit modication. All systems, regardless of their size and
capacity, should have appropriate recirculation and turnover to assure the system
is well controlled chemically and microbiologically.
2.3 The use of the systems following initial validation (installation qualication
(IQ), operational qualication (OQ) and performance qualication (PQ)) and aer
any planned and unplanned maintenance or modication work should be approved
by the quality assurance (QA) department using change control documentation.
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2.4 Water sources and treated water should be monitored regularly for
chemical, microbiological and, as appropriate, endotoxin contamination. e
performance of water purication, storage and distribution systems should also
be monitored. Records of the monitoring results, trend analysis and any actions
taken should be maintained.
2.5 Where chemical sanitization of the water systems is part of the biocon-
tamination control programme a validated procedure should be followed to en-
sure that the sanitizing process has been eective and that the sanitizing agent has
been eectively removed.
3. Water quality specifications
3.1 General
3.1.1 e following requirements concern water processed, stored and distributed
in bulk form. ey do not cover the specication of water formulated for patient
administration. Pharmacopoeias include specications for both bulk and dosage-
form types of water.
3.1.2 Pharmacopoeial requirements or guidance for WPU are described
in national, regional and international pharmacopoeias and limits for various
impurities or classes of impurities are either specied or recommended.
Companies wishing to supply multiple markets should set specications that
meet the strictest requirements from each of the relevant pharmacopoeias.
Similarly, requirements or guidance are given in pharmacopoeias on the
microbiological quality of water.
3.2 Drinking-water
3.2.1 Drinking-water should be supplied under continuous positive pressure in a
plumbing system free of any defects that could lead to contamination of any product.
3.2.2 Drinking-water is unmodied except for limited treatment of the water
derived from a natural or stored source. Examples of natural sources include
springs, wells, rivers, lakes and the sea. e condition of the source water will
dictate the treatment required to render it safe for human consumption (drink-
ing). Typical treatment includes desalinization, soening, removal of specic
ions, particle reduction and antimicrobial treatment.
3.2.3 It is common for drinking-water to be derived from a public water supply
that may be a combination of more than one of the natural sources listed above.
It may also be supplied either from an osite source, e.g. a municipality, or ap-
propriate quality may be achieved onsite through appropriate processing.
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3.2.4 It is also common for public water supply organizations to conduct tests
and guarantee that the drinking-water delivered is of drinking quality. is test-
ing is typically performed on water from the water source.
3.2.5 It is the responsibility of the pharmaceutical manufacturer to assure that
the source water supplying the puried water (PW) treatment system meets the
appropriate drinking-water requirements. ere may be situations where the
water treatment system is used rst to achieve drinking-water quality and sub-
sequently puried water. In these situations the point at which drinking-water
quality is achieved should be identied and tested.
3.2.6 Drinking-water quality is covered by the WHO drinking-water guide-
lines, standards from the International Organization for Standardization (ISO)
and other regional and national agencies. Drinking-water should comply with
the relevant regulations laid down by the competent authority.
3.2.7 If drinking-water is used directly in certain stages of pharmaceutical
manufacture or is the feed-water for the production of higher qualities of WPU,
then testing should be carried out periodically by the water user’s site to con-
rm that the quality meets the standards required for drinking-water.
3.3 Bulk purified water
3.3.1 Bulk puried water (BPW) should be prepared from a drinking-water source
as a minimum-quality feed-water. It should meet the relevant pharmacopoeial
specications for chemical and microbiological purity with appropriate action
and alert limits. It should also be protected from recontamination and microbial
proliferation. BPW may be prepared by a combination of reverse osmosis (RO)
RO/electro-deionization (EDI) and vapour compression (VC). Alert levels for
the water system should be determined from knowledge of the system and are
not specied in the pharmacopoeias.
3.4 Bulk highly purified water
3.4.1 Bulk highly puried water (BHPW) should be prepared from drinking-
water as a minimum-quality feed-water. BHPW is a unique specication for
water found only in the European Pharmacopoeia. is grade of water must
meet the same quality standard as water for injections (WFI), including the limit
for endotoxins, but the water-treatment process used may be dierent. Current
production methods include, for example, double-pass RO coupled with other
suitable techniques such as ultraltration and deionization.
BHPW may be prepared by a combination of dierent methods such as
RO, ultraltration and deionization.
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3.4.2 BHPW should also be protected from recontamination and microbial
proliferation.
3.4.3 BHPW and WFI have identical microbiological requirements.
3.5 Bulk water for injections
3.5.1 Bulk water for injections (BWFI) should be prepared from drinking-water
(usually with further treatment) or puried water as a minimum-quality feed-
water. BWFI is not sterile water and is not a nal dosage form. It is an intermediate
bulk product and suitable to be used as an ingredient during formulation. BWFI
is the highest quality of pharmacopoeial WPU.
3.5.2 Certain pharmacopoeias place constraints upon the permitted puri-
cation techniques as part of the specication of the BWFI. e International
Pharmacopoeia and the European Pharmacopoeia, for example, allow only distil-
lation as the nal purication step.
3.5.3 BWFI should meet the relevant pharmacopoeial specications for chemi-
cal and microbiological purity (including endotoxin) with appropriate action and
alert limits.
3.5.4 BWFI should also be protected from recontamination and microbial
proliferation.
3.6 Other grades of water
3.6.1 When a specic process requires a special non-pharmacopoeial grade of
water, its specication must be documented within the company quality system.
As a minimum it must meet the pharmacopoeial requirements relating to the
grade of WPU required for the type of dosage form or process step.
4. Application of specific types of water
to processes and dosage forms
4.1 Product licensing authorities specify the minimum grade of WPU that must
be used during the manufacture of the dierent dosage forms or for dierent
stages in washing, preparation, synthesis, manufacturing or formulation.
4.2 The grade of water used should take into account the nature and intended
use of the intermediate or nished product and the stage in the manufacturing
process at which the water is used.
4.3 BHPW can be used in the preparation of products when water of high
quality (i.e. very low in microorganisms and endotoxins) is needed, but the
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process stage or product requirement does not include the constraint on the
production method defined in some of the pharmacopoeial monographs for
BWFI.
4.4 BWFI should be used in the manufacture of injectable products for
dissolving or diluting substances or preparations during the manufacturing of
parenterals, and for manufacture of sterile water for preparation of injections.
BWFI should also be used for the nal rinse aer cleaning of equipment and
components that come into contact with injectable products as well as for the
nal rinse in a washing process in which no subsequent thermal or chemical
depyrogenization process is applied.
4.5 When steam comes into contact with an injectable product in its nal
container or with equipment for preparing injectable products, it should conform
to the specication for BWFI when condensed.
5. Water purification systems
5.1 General considerations
5.1.1 e specications for WPU found in compendia (e.g. pharmacopoeias) do
not dene the permissible water purication methods apart from for BWFI (refer
to section 3.5).
5.1.2 e chosen water purication method or sequence of purication steps
must be appropriate to the application in question. e following should be con-
sidered when selecting the water treatment method:
– the nal water quality specication;
– the quantity of water required by the user;
– the available feed-water quality and the variation over time
(seasonal changes);
– the availability of suitable support facilities for system connection
(raw water, electricity, heating steam, chilled water, compressed
air, sewage system, exhaust air);
– the sanitization strategy;
– the availability of water-treatment equipment on the market;
– the reliability and robustness of the water-treatment equipment
in operation;
– the yield or eciency of the purication system;
– the ability to adequately support and maintain the water
purication equipment;
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– the continuity of operational usage considering hours/days, days/
years and planned downtime;
– the total life-cycle costs (capital and operational including
maintenance).
5.1.3 e specications for water purication equipment, storage and
distribution systems should take into account the following:
– the location of the plant room;
– extremes in temperature that the system will encounter;
– the risk of contamination from leachates from contact materials;
– the adverse impact of adsorptive contact materials;
– hygienic or sanitary design, where required;
– corrosion resistance;
– freedom from leakage;
– a system conguration to avoid proliferation of microbiological
organisms;
– tolerance to cleaning and sanitizing agents (thermal and/or
chemical);
– the sanitization strategy;
– the system capacity and output requirements;
– the provision of all necessary instruments, test and sampling
points to allow allthe relevant critical quality parameters of the
complete system to be monitored.
5.1.4 e design, conguration and layout of the water purication equipment,
storage and distribution systems should also take into account the following
physical considerations:
– ability to collect samples;
– the space available for the installation;
– structural loadings on buildings;
– the provision of adequate access for maintenance;
– the ability to safely handle regeneration and sanitization chemicals.
5.2 Production of drinking-water
5.2.1 Drinking-water is derived from a raw water source such as a well, river or
reservoir. ere are no prescribed methods for the treatment of raw water to
produce drinking-water from a specic raw water source.
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5.2.2 Typical processes employed at a user plant or by a water supply authority
include:
– desalinization;
– ltration;
– soening;
– disinfection or sanitization (e.g. by sodium hypochlorite
(chlorine) injection);
– iron (ferrous) removal;
– precipitation;
– reduction of concentration of specic inorganic and/or organic
materials.
5.2.3 e drinking-water quality should be monitored routinely to account for
environmental, seasonal or supply changes which have an impact on the source
water quality.
5.2.4 Additional testing should be considered if there is any change in the raw-
water source, treatment techniques or system conguration.
5.2.5 Trend review may be used to identify changes. If the drinking-water
quality changes signicantly, but is still within specication, the direct use of this
water as a WPU, or as the feed-water to downstream treatment stages, should be
reviewed and the result of the review documented.
5.2.6 Where drinking-water is derived from an “in-house” system for
the treatment of raw water, the water-treatment steps used and the system
conguration should be documented. Changes to the system or to its operation
should not be made until a review has been completed and the change approved
by the QA department in accordance with change control procedures.
5.2.7 Where drinking-water is stored and distributed by the user, the storage
systems must not allow degradation of the water quality before use. Aer any
such storage, testing should be carried out routinely in accordance with a dened
method. Where water is stored, the system design and operation should ensure a
turnover or recirculation of the stored water sucient to prevent stagnation.
5.2.8 e drinking-water system is usually considered to be an “indirect impact
system” and does not need to be qualied.
5.2.9 Drinking-water purchased in bulk and transported to the user by tanker
has additional problems and risks not associated with drinking-water delivered
by pipeline. Vendor assessment and authorized certication activities, including
conrmation of the acceptability of the delivery vehicle, should be undertaken in
a similar way to that used for any other starting material.
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5.2.10 Equipment and systems used to produce drinking-water should be able to be
drained and sanitized. Storage tanks should be closed with appropriately protected
vents, and should allow for visual inspection and for being drained and sanitized.
Distribution pipework should be able to be drained or ushed and sanitized.
5.2.11 Special care should be taken to control microbiological contamination
of sand lters, carbon beds and water soeners. Once microorganisms have
infected a system, the contamination can rapidly form biolms and spread
throughout the system. Techniques for controlling contamination such as back-
ushing, chemical and/or thermal sanitization and frequent regeneration should
be considered as appropriate.
5.3 Production of purified water
5.3.1 Any appropriate qualied purication technique or sequence of techniques
may be used to prepare puried water (PW). PW is commonly produced by ion
exchange, RO, ultraltration and/or electro-deionization processes and distillation.
5.3.2 e following should be considered when conguring a water
purication system or dening user requirement specications (URS):
– the feed-water quality and its variation over seasons;
– the quantity of water required by the user;
– the required water-quality specication;
– the sequence of purication stages required;
– the energy consumption;
– the extent of pretreatment required to protect the nal purication
steps;
– performance optimization, including yield and eciency of unit
treatment-process steps;
– appropriately located sampling points designed in such a way as
to avoid potential contamination;
– unit process steps should be provided with appropriate
instrumentation to measure parameters such as ow, pressure,
temperature, conductivity, pH and total organic carbon.
5.3.3 Ambient-temperature systems such as ion exchange, RO and ultraltration
are especially susceptible to microbiological contamination, particularly when equip-
ment is static during periods of no or low demand for water. It is essential to consider
the mechanisms for microbiological control and sanitization.
e method for sanitizing each stage of purication needs to be dened
and must include verication of the removal of any agents used. ere should be
documented evidence of its ecacy.
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5.3.4 e following should be considered:
– maintenance of minimum ow through the water generation
system is recommended at all times;
– control of temperature in the system by heat exchanger or plant-
room cooling to reduce the risk of microbial growth (guidance
value < 25 °C);
– provision of ultraviolet disinfection;
– selection of water-treatment components that can periodically be
thermally sanitized;
– application of chemical sanitization (including agents such as
ozone, hydrogen peroxide and/or peracetic acid);
– thermal sanitization at > 65 °C.
5.4 Production of highly purified water
5.4.1 Highly puried water (HPW) can be produced by double-pass reverse
osmosis coupled with ultraltration or by any other appropriate qualied
purication technique or sequence of techniques.
5.4.2 e guidance provided in section 5.3 for PW is equally applicable to
HPW.
5.5 Production of water for injection(s)
5.5.1 Some pharmacopoeias prescribe or limit the permitted nal water
purication stage in the production of BWFI. Distillation is the preferred
technique; it is considered a more robust technique based on phase change, and
in some cases, high-temperature operation of the process equipment.
5.5.2 e following should be considered when designing a water purication
system and dening URS:
– the feed-water quality;
– the required water quality specication;
– the quantity of water;
– the optimum generator size or generators with variable control to
avoid over-frequent start/stop cycling;
– blow-down and dump functions;
– cool-down venting to avoid contamination ingress.
5.5.3 e system conguration guidance provided in section 5.3 for PW is
equally applicable to water for injection.
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6. Water storage and distribution systems
6.1 is section applies to WPU systems for PW, BHPW and BWFI. e water
storage and distribution should work in conjunction with the purication plant
to ensure delivery of water of consistent quality to the user points, and to ensure
optimum operation of the water purication equipment.
6.1 General
6.1.1 e storage and distribution system should be considered as a key part of
the whole system and should be designed to be fully integrated with the water
purication components of the system.
6.1.2 Once water has been purified using an appropriate method it can
either be used directly or, more frequently, it will be fed into a storage vessel
for subsequent distribution to points of use. The following text describes the
requirements for storage and distribution systems and point of use (POU).
6.1.3 e storage and distribution system should be congured to prevent
microbial proliferation and recontamination of the water (PW, BHPW, BWFI)
aer treatment. It should be subjected to a combination of online and oine
monitoring to ensure that the appropriate water specication is maintained.
6.2 Materials that come into contact with systems
for water for pharmaceutical use
6.2.1 is section applies to generation equipment for PW, BHPW and BWFI and
the associated storage and distribution systems.
6.2.2 e materials that come into contact with WPU, including pipework,
valves and ttings, seals, diaphragms and instruments, should be selected to
satisfy the following objectives.
■ Compatibility. e compatibility and suitability of the materials
should encompass the full range of its working temperature and
potential chemicals that will come into contact with the system at
rest, in operation and during sanitization.
■ Prevention of leaching. All materials that come into contact with WPU
should be non-leaching at the range of working and sanitization
temperatures of the system.
■ Corrosion resistance. PW, BHPW and BWFI are highly corrosive.
To prevent failure of the system and contamination of the water, the
materials selected must be appropriate, the method of jointing must be carefully
controlled and all ttings and components must be compatible with the pipework
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used. Appropriate sanitary specication plastics and stainless-steel materials are
acceptable for WPU systems.
When stainless steel is used it should be at least grade 316. In general
316L or a higher grade of stainless steel is used.
e system should be passivated aer initial installation or aer signicant
modication. When accelerated passivation is undertaken the system should be
thoroughly cleaned rst and the passivation process should be undertaken in
accordance with a clearly dened documented procedure.
■ Smooth internal nish. Once water has been puried it is susceptible to
microbiological contamination and the system is subject to the formation
of biolms when cold storage and distribution are employed. Smooth
internal surfaces help to avoid roughness and crevices within the WPU
system. Crevices can be the source of contamination because of possible
accumulation of microorganisms and formation of biolms. Crevices are
also frequently sites where corrosion can commence. e internal material
nish should have an arithmetical average surface roughness of not
greater than 0.8 micrometre (Ra). When stainless steel is used, mechanical
and electro-polishing techniques may be employed. Electro-polishing
improves the resistance of the stainless-steel material to surface corrosion.
■ Jointing. e selected system materials should be easily joined by
welding in a controlled manner. e control of the process should
include, as a minimum, qualication of the operator, documentation
of the welder set-up, work session test pieces (coupons), logs of all
welds and visual inspection of a dened proportion of welds, e.g.
100% hand welds, 10% automatic welds.
■ Design of anges, unions and valves. Where anges, unions or valves
are used they should be of a hygienic or sanitary design. Appropriate
checks should be carried out to ensure that the correct seals and
diaphragms are used and that they are tted and tightened correctly.
readed connections should be avoided.
■ Documentation. All system components should be fully documented
and be supported by original or certied copies of material certicates.
■ Materials. Suitable materials that may be considered for sanitary
elements of the system include 316L (low carbon) stainless steel,
polypropylene, polyvinylidene-diuoride and peruoroalkoxy. e
choice of material should take into account the intended sanitization
method. Other materials such as unplasticized polyvinyl-chloride
(uPVC) may be used for treatment equipment designed for less pure
water such as ion exchangers and soeners.
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None of the materials that come into contact with WPU should contain
chemicals that will be extracted by the water. Plastics should be non-toxic and
should be compatible with all chemicals used. ey should be manufactured
from materials that should at least meet minimum food grade standards. eir
chemical and biological characteristics should meet any relevant pharmacopoeia
specications or recommendations.
Precautions should be taken to dene operational limits for areas where
water circulation is reduced and turbulent ow cannot be achieved. Minimum
ow rate and change volumes should be dened.
6.3 System sanitization and bioburden control
6.3.1 Water treatment equipment, storage and distribution systems used for BPW,
BHPW and BWFI should be provided with features to control the proliferation
of microbiological organisms during normal use, as well as techniques for
sanitizing the system aer intervention for maintenance or modi cation. e
techniques employed should be considered during the design of the system and
should take into account the interdependency between the materials and the
sanitization techniques.
6.3.2 Systems that operate and are maintained at elevated temperatures
(e.g. > 65) are generally less susceptible to microbiological contamination
than systems that are maintained at lower temperatures. When lower
temperatures are required due to the water treatment processes employed
or the temperature requirements for the water in use, special precautions
should be taken to prevent the ingress and proliferation of microbiological
contaminants (see section 6.4.3 for guidance).
6.4 Storage vessel requirements
6.4.1 General
6.4.1.1 The water storage vessel used in a system serves a number of important
functions. The design and size of the vessel should take into consideration
the following.
6.4.2 Capacity
6.4.2.1 e capacity of the storage vessel should be determined on the basis of the
following requirements:
■ It is necessary to provide a buer capacity between the steady-state
generation rate of the water-treatment equipment and the potentially
variable simultaneous demand from user points.
■ e water-treatment equipment should be able to operate
continuously for signicant periods to avoid the ineciencies and
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equipment stress that occur when the equipment cycles on and o
too frequently.
■ e capacity should be sucient to provide short-term reserve
capacity in the event of failure of the water-treatment equipment or
inability to produce water due to a sanitization or regeneration cycle.
When determining the size of such reserve capacity, consideration
should be given to providing sucient water to complete a process
batch, work session, tank turnover by recirculation to minimize
stagnation, or other logical period of demand.
6.4.3 Contamination control considerations
6.4.3.1 e following should be taken into account for the ecient control of
contamination:
■ e headspace in the storage vessel is an area of risk where water
droplets and air can come into contact at temperatures that encourage
the proliferation of microbiological organisms. e use of spray-ball
or distributor devices should be considered in these systems to wet
the surfaces during normal operation, chemical and/or thermal
sanitization.
■ Nozzles within the storage vessels should be congured to avoid dead
zones where microbiological contamination might be harboured.
■ Vent lters are tted to storage vessels to allow the internal level
of liquid to uctuate. e lters should be bacteria-retentive,
hydrophobic and should ideally be congured to allow in situ testing
of integrity. Oine testing is also acceptable. e use of heated vent
lters should be considered for continuous hot storage or systems
using periodic heat sanitization to prevent condensation within the
lter matrix that might lead to lter blockage and to microbial growth
that could contaminate the storage vessels.
■ Where pressure-relief valves and bursting discs are provided on
storage vessels to protect them from under- and over-pressurization,
these devices should be of a sanitary design. Bursting discs should
be provided with external rupture indicators to ensure that loss of
system integrity is detected.
6.5 Requirements for water distribution pipework
6.5.1 General
6.5.1.1 e distribution of BPW, BHPW and BWFI should be accomplished using
a continuously circulating pipework loop. Proliferation of contaminants within
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the storage tank and distribution loop should be controlled. Good justication
for using a non-recirculating one-way system should be provided.
6.5.1.2 Filtration should not usually be used in distribution loops or at take
o-user points to control biocontamination. Such lters are likely to conceal
system contamination.
6.5.2 Temperature control and heat exchangers
6.5.2.1 Where heat exchangers are employed to heat or cool WPU within a system,
precautions should be taken to prevent the heating or cooling utility from
contaminating the water. e more secure types of heat exchangers of the double
tube plate or double plate and frame or tube and shell conguration should be
considered. Where these types are not used, an alternative approach whereby the
utility is maintained and monitored at a lower pressure than the WPU may be
considered. e latter approach is not usually adopted in BWFI systems.
6.5.2.2 Where heat exchangers are used they should be arranged in
continually circulating loops or subloops of the system to avoid unacceptable
static water in systems.
6.5.2.3 When the temperature is reduced for processing purposes the reduction
should occur for the minimum necessary time. e cooling cycles and their dura-
tion should be proven satisfactory during the qualication of the system.
6.5.3 Circulation pumps
6.5.3.1 Circulation pumps should be of a sanitary design with appropriate
seals that prevent contamination of the system. Where stand-by pumps are
provided, they should be configured or managed to avoid dead zones trapped
within the system.
Consideration should be given to preventing contamination in systems
where parallel pump systems are used, especially if there is stagnant water when
one of the pumps is not being used.
6.5.4 Biocontamination control techniques
6.5.4.1 Water purication systems should be sanitized using chemical or thermal
sanitization procedures as appropriate (production and distribution). e proce-
dure and conditions used (such as times and temperatures) should be suitable.
6.5.4.2 e following control techniques may be used alone or more commonly
in combination:
■ maintenance of continuous turbulent flow circulation within
water distribution systems reduces the propensity for the
formation of biofilms;
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■ the system design should ensure the shortest possible length of
pipework;
■ for ambient temperature systems, pipework should be isolated from
adjacent hot pipes;
■ deadlegs in the pipework should be minimized through appropriate
design, and as a guide should not signicantly exceed three times the
branch diameter as measured from the ID pipe wall to centre line of
the point-of-use valve where signicant stagnation potential exists;
■ pressure gauges should be separated from the system by membranes;
■ hygienic pattern diaphragm valves should be used;
■ pipework for steam-sanitized systems should be sloped and fully
drainable;
■ the growth of microorganisms can be inhibited by:
– ultraviolet radiation sources in pipework;
– maintaining the system heated (greater than 65 °C);
– sanitizing the system periodically using hot water (guidance
temperature > 70°C);
– sanitizing the system periodically using superheated hot water or
clean steam;
– routine chemical sanitization using ozone or other suitable
chemical agents. When chemical sanitization is used, it is essential
to prove that the agent has been removed prior to using the water.
Ozone can be eectively removed by using ultraviolet radiation.
7. Operational considerations
7.1 Start-up and commissioning of water systems
7.1.1 Planned, well-dened, successful and well-documented commissioning and
qualication is an essential precursor to successful validation of water systems.
7.1.2 e commissioning work should include setting to work, system set-up,
controls, loop tuning and recording of all system performance parameters. If it is
intended to use or to refer to commissioning data within the validation work then
the quality of the commissioning work and associated data and documentation
must be commensurate with the validation plan requirements.
7.2 Qualification
7.2.1 WPU, BPW, BHPW and BWFI systems are all considered to be direct
impact, quality critical systems that should be qualied. e qualication
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should follow the validation convention of design review or design qualication
(DQ), IQ, OQ, and PQ.
7.2.2 is guidance does not dene the standard requirements for the conven-
tional qualication stages DQ, IQ and OQ, but concentrates on the particular PQ
approach that should be used for WPU systems to demonstrate their consistent
and reliable performance. A three-phase approach should be used to satisfy the
objective of proving the reliability and robustness of the system in service over an
extended period.
Tests on the source water must be included within the validation
programme and continued as part of the routine monitoring. e source water
should meet the requirements for drinking-water and any internal specication.
Phase 1. Sample daily or continuously monitor the incoming feed-water
to verify its quality.
A test period of two weeks should be spent monitoring the system
intensively. During this period, the system should operate continuously
without failure or performance deviation. Usually water is not used for nished
pharmaceutical product (FPP) manufacturing during this period. e following
activities should be included in the testing approach.
■ Undertake chemical and microbiological testing in accordance with
a dened plan.
■ Sample or continuously monitor the incoming feed-water daily to
verify its quality.
■ Sample or continuously monitor aer each step in the purication process.
■ Sample or continuously monitor at each point of use and at other
dened sample points.
■ Develop appropriate operating ranges.
■ Develop and nalize operating, cleaning, sanitizing and maintenance
procedures.
■ Demonstrate production and delivery of product water of the
required quality and quantity.
■ Use and rene the standard operating procedures (SOPs) for
operation, maintenance, sanitization and troubleshooting.
■ Verify provisional alert levels.
■ Develop and rene test-failure procedure.
Phase 2. A further test period of two weeks should be spent carrying
out further intensive monitoring while deploying all the rened SOPs aer the
satisfactory completion of phase 1. e sampling scheme should be generally the
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same as in phase 1. Use of the water for FPP manufacturing purposes during this
phase may be acceptable, provided that both commissioning and phase 1 data
demonstrate appropriate water quality and the practice is approved by QA. e
approach should also:
– demonstrate consistent operation within established ranges;
– demonstrate consistent production and delivery of water of the
required quantity and quality when the system is operated in
accordance with the SOPs.
Phase 3. Phase 3 typically runs for one year aer the satisfactory completion
of phase 2. Water can be used for FFP manufacturing purposes during this phase
which has the following objectives:
■ to demonstrate reliable performance over an extended period;
■ to ensure that seasonal variations are evaluated.
e sample locations, sampling frequencies and tests should be reduced
to the normal routine pattern based on established procedures proven during
phases 1 and 2.
7.3 Continuous system monitoring
7.3.1 Aer completion of phase 3 of the qualication programme for the WPU
system, a system review should be undertaken. Following this review a routine
monitoring plan should be established based on the results of phase 3.
Monitoring should include a combination of monitoring with online
instruments (with appropriately qualied alarm systems) of parameters such as
ow, pressure, temperature, conductivity and total organic carbon, and oine
sample testing for physical, chemical and microbiological attributes. Oine
samples should be taken from points of use or dedicated sample points where
points of use cannot be sampled. All water samples should be taken using the
same methodology as detailed in production procedures. ere should be a
suitable ushing and drainage procedure in place.
7.3.2 Tests should be carried out to ensure that the approved pharmacopoeial
and company specication has been met.
is may include the microbiological quality of water as appropriate.
Monitoring data should be subject to trend analysis (trending should
typically be within 2 sigma). Suitable alert and action levels should be established
based on historical reported data.
7.3.3 Any trend towards frequently exceeding alert limits should trigger a thor-
ough investigation of the root cause, followed by appropriate corrective actions.
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7.4 Maintenance of water systems
7.4.1 WPU systems should be maintained in accordance with a controlled,
documented maintenance programme that takes into account the following:
– dened frequency for system elements;
– the calibration programme;
– SOPs for specic tasks;
– control of approved spares;
– issue of a clear maintenance plan and instructions;
– review and approval of systems for use upon completion of work;
– record and review of problems and faults during maintenance.
7.5 System reviews
7.5.1 WPU (BPW, BHPW and BWFI) systems should be reviewed at appropriate
regular intervals. e review team should comprise representatives from
engineering, QA, microbiology, operations and maintenance. e review should
consider matters such as:
– changes made since the last review;
– system performance;
– reliability;
– quality trends;
– failure events;
– investigations;
– out-of-specications results from monitoring;
– changes to the installation;
– updated installation documentation;
– log books;
– the status of the current SOP list.
7.5.2 For new systems, or systems that display instability or unreliability, the
following should also be reviewed:
– need for investigation;
– corrective actions and preventative actions (CAPA);
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– qualication (DQ, factory acceptance test (FAT), IQ, site
acceptance test (SAT), OQ, PQ) or equivalent verication
documents, and monitoring phases of the system.
8. Inspection of water systems
8.1 WPU (BPW, BHPW and BWFI) systems are likely to be the subject of
regulatory inspection from time to time. Users should consider conducting
routine audit and self-inspection of established water systems.
8.2 This GMP guidance can be used as the basis of inspection. A tour of the
water generation plant and visible pipework (including user points) should be
performed to ensure that the system is appropriately designed, installed and
maintained (e.g. that there are no leaks and that the system matches the piping
and instrumentation diagram or drawing (P&ID).
e following list identies items and a logical sequence for a WPU
system inspection or audit:
– a current drawing of the water system showing all equipment in
the system from the inlet to the points of use along with sampling
points and their designations;
– approved piping drawings (e.g. orthographic and/or isometric);
– a sampling and monitoring plan with a drawing of all sample
points;
– training programme for sample collection and testing;
– the setting of monitoring alert and action levels;
– monitoring results and evaluation of trends;
– inspection of the last annual system review;
– review of any changes made to the system since the last audit and
a check that the change control has been implemented;
– review of deviations recorded and their investigation;
– general inspection of system for status and condition;
– review of maintenance, failure and repair logs;
– checking calibration and standardization of critical instruments.
8.3 For an established system that is demonstrably under control this scope of
review should prove adequate.
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Further reading
e International Pharmacopoeia. Geneva, World Health Organization; http://
www.who.int/medicines/publications/pharmacopoeia/overview/en/index.html.
WHO guidelines on good manufacturing practices: validation. In: WHO Expert
Committee on Specications for Pharmaceutical Preparations. Fortieth report.
Geneva, World Health Organization, 2006, Annex 4 (WHO Technical Report
Series, No. 937); http://www.who.int/medicines/publications/pharmprep/
TRS_937.pdf#page=119.
WHO Guidelines for drinking-water quality, 3rd edition. Geneva, World Health
Organization, 2008; http://www.who.int/water_sanitation_health/dwq/
gdwq3rev/en/index.html.
American Society of Mechanical Engineers. Bioprocessing Equipment Standard.
ASME — BPE 2000.
Banes PH. Passivation; understanding and performing procedures on austenitic
stainless steel systems. Pharmaceutical Engineering, 1990: 41.
Guide to inspections of high purity water systems. Maryland, US Food and Drug
Administration, 1993; http://www.fda.gov/ICECI/InspectionGuides.
Biotechnology. Equipment. Guidance on testing procedures for cleanability. British
Standards Publishing. BS EN 12296, 1998.
European Medicines Agency. Note for guidance on the quality of water for
pharmaceutical use. London, 2002 (CPMP/QWP/158-01); http://www.emea.
europa.eu/docs/en_GB/document_library/Scientific_guideline/2009/09/
WC500003394.pdf.
European Pharmacopoeia: see web site for the publishers of the European
Pharmacopoeia and supplements; http://www.pheur.org/.
Harfst WH. Selecting piping materials for high-purity water systems. Ultra Pure
Water, May/June 1994.
ISPE Good practice guide: commissioning and qualication of pharmaceutical
water and steam systems. ISPE Baseline TM Pharmaceutical Engineering Guide,
Vol. 4. International Society for Pharmaceutical Engineering, 2007.
ISPE Baseline Guide Volume 4: Water and Steam Systems. International Society
for Pharmaceutical Engineering, 2001.
Noble PT. Transport considerations for microbial control in piping. Journal of
Pharmaceutical Science and Technology, 1994, 48: 76–85.
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Pharmaceutical Inspection Co-operation Scheme. PIC/S; Inspection of utilities;
P1 009-1. Geneva, Pharmaceutical Inspection Co-operation Scheme, 2002.
Tverberg JC, Kerber SJ. Eect of nitric acid passivation on the surface composition
of mechanically polished type 316 L sanitary tube. European Journal of Parenteral
Sciences, 1998, 3: 117–124.
US Food and Drug Administration. Guide to inspections of high purity water
systems, high purity water systems (7/93), 2009; http://www.fda.gov/ICECI/
Inspections/InspectionGuides/ucm074905.htm.
US Pharmacopeia: Published annually; see http://www.usp.org/.
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