Guidelines for performance evaluation of treatment technologies for water reuse systems — Part 3: Ozone treatment technology

This document specifies performance evaluation methods of treatment technology using ozone for water reuse systems. It deals with how to measure typical parameters which indicate performance of ozone treatment technology.

Lignes directrices pour l’évaluation des performances des techniques de traitement des systèmes de réutilisation de l’eau — Partie 3: Technique de traitement à l'ozone

General Information

Status
Published
Publication Date
24-Jun-2020
Current Stage
6060 - International Standard published
Start Date
25-Jun-2020
Due Date
06-Oct-2020
Completion Date
25-Jun-2020
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INTERNATIONAL ISO
STANDARD 20468-3
First edition
2020-06
Guidelines for performance evaluation
of treatment technologies for water
reuse systems —
Part 3:
Ozone treatment technology
Lignes directrices pour l’évaluation des performances des techniques
de traitement des systèmes de réutilisation de l’eau —
Partie 3: Technique de traitement à l'ozone
Reference number
ISO 20468-3:2020(E)
©
ISO 2020

---------------------- Page: 1 ----------------------
ISO 20468-3:2020(E)

COPYRIGHT PROTECTED DOCUMENT
© ISO 2020
All rights reserved. Unless otherwise specified, or required in the context of its implementation, no part of this publication may
be reproduced or utilized otherwise in any form or by any means, electronic or mechanical, including photocopying, or posting
on the internet or an intranet, without prior written permission. Permission can be requested from either ISO at the address
below or ISO’s member body in the country of the requester.
ISO copyright office
CP 401 • Ch. de Blandonnet 8
CH-1214 Vernier, Geneva
Phone: +41 22 749 01 11
Email: copyright@iso.org
Website: www.iso.org
Published in Switzerland
ii © ISO 2020 – All rights reserved

---------------------- Page: 2 ----------------------
ISO 20468-3:2020(E)

Contents Page
Foreword .iv
Introduction .v
1 Scope . 1
2 Normative references . 1
3 Terms, definitions and abbreviated terms . 1
3.1 Terms and definitions . 1
3.2 Abbreviated terms . 2
4 System configuration . 2
4.1 General . 2
4.2 Ozone system for water treatment . 3
4.2.1 Feed gas supply unit. 3
4.2.2 Ozone generation unit . 3
4.2.3 Ozone contact unit . . 3
4.2.4 Off-gas ozone treatment unit . 3
4.2.5 Ozone measuring system . 4
5 Principles and general guidelines for performance evaluation . 4
5.1 General . 4
5.2 Functional requirements . 4
5.2.1 General. 4
5.2.2 Performance evaluation procedures . 5
5.3 Non-functional requirements . 7
5.3.1 Performance characteristics . 7
5.3.2 Environmental and economic key factors . 7
5.3.3 Safety requirements . 8
Annex A (informative) Main treatment technologies and target constituents for water reuse .9
Annex B (informative) Reuse water quality parameters .10
Annex C (informative) Ozone concentration monitoring points .23
Annex D (informative) Ozone generation control methods .25
Bibliography .26
© ISO 2020 – All rights reserved iii

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ISO 20468-3:2020(E)

Foreword
ISO (the International Organization for Standardization) is a worldwide federation of national standards
bodies (ISO member bodies). The work of preparing International Standards is normally carried out
through ISO technical committees. Each member body interested in a subject for which a technical
committee has been established has the right to be represented on that committee. International
organizations, governmental and non-governmental, in liaison with ISO, also take part in the work.
ISO collaborates closely with the International Electrotechnical Commission (IEC) on all matters of
electrotechnical standardization.
The procedures used to develop this document and those intended for its further maintenance are
described in the ISO/IEC Directives, Part 1. In particular, the different approval criteria needed for the
different types of ISO documents should be noted. This document was drafted in accordance with the
editorial rules of the ISO/IEC Directives, Part 2 (see www .iso .org/ directives).
Attention is drawn to the possibility that some of the elements of this document may be the subject of
patent rights. ISO shall not be held responsible for identifying any or all such patent rights. Details of
any patent rights identified during the development of the document will be in the Introduction and/or
on the ISO list of patent declarations received (see www .iso .org/ patents).
Any trade name used in this document is information given for the convenience of users and does not
constitute an endorsement.
For an explanation of the voluntary nature of standards, the meaning of ISO specific terms and
expressions related to conformity assessment, as well as information about ISO's adherence to the
World Trade Organization (WTO) principles in the Technical Barriers to Trade (TBT), see www .iso .org/
iso/ foreword .html.
This document was prepared by Technical Committee ISO/TC 282, Water reuse, Subcommittee SC 3,
Risk and performance evaluation of water reuse system.
A list of all parts in the ISO 20468 series can be found on the ISO website.
Any feedback or questions on this document should be directed to the user’s national standards body. A
complete listing of these bodies can be found at www .iso .org/ members .html.
iv © ISO 2020 – All rights reserved

---------------------- Page: 4 ----------------------
ISO 20468-3:2020(E)

Introduction
The rapidly growing global market for water reuse technologies inevitably demands standards which
are applicable on a world-wide basis. Many regions in the world are facing water shortages, and there is
great interest in the use of technologies that can treat wastewater and make the reuse water available
for a wide range of reuse applications that can satisfy non-potable water demands, thereby conserving
precious potable water supplies. Simultaneously, the implementation of water reuse schemes is raising
public and regulatory concerns regarding potential human health, environmental and societal impacts.
This has led to an increasing need to specify various aspects of water reuse projects and there is a
growing need on behalf of regulators, reuse technology suppliers, and users of those technologies for
international standardization. Without ISO water reuse standards, a great number of opportunities for
sustainable development based on water reuse will be lost.
Standardization needs to include objective specification and evaluation of levels of service and water
reuse system performance dependability, including safety, environmental protection, and resilience and
cost-effectiveness considerations. Hence, appropriate methods are needed to evaluate the performance
of water reuse systems.
The performance of treatment technologies for water reuse, inter alia, should be evaluated properly in
order to select the most appropriate technologies in an unbiased way to achieve the objectives of the
water reuse project. Despite considerable research and development on treatment technologies, such
scientific knowledge is largely held within commercial interests. Given less than ideal communication
between producers and users of reuse technologies with regards to treatment performance, clear
information as to what to measure on the one hand and what level of performance is required on the
other is currently missing. To address these challenges, this document provides methods and tools,
which can be accepted by most stakeholders, to evaluate the performance of treatment technologies for
water reuse systems from multitude of applications.
Based on the discussion in the meetings of ISO/TC 282/SC 3, ISO 20468-1 titled “Guidelines for
performance evaluation of treatment technologies for water reuse systems — Part 1: General” has been
developed to establish the standard of generic aspects for performance evaluation. In this context,
this document stipulating specific ways of performance evaluation of ozone treatment technology,
commonly known as ozonation, for water reuse systems, based on ISO 20468-1 as the generic standard,
is established herein.
Ozone (O ) is an allotrope of oxygen (O ) and is the second strongest oxidiser after fluorine. Its strong
3 2
oxidative decomposition power makes it effective as a disinfectant and in removal of oxidizable
constituents in water. There are cases where ozonation at high doses is used to remove micro-pollutants
in wastewater for environmental protection.
In various types of water reuse systems, the disinfection and the removal of colour and odour are
essential. Then it can be said that ozone technology plays an important role to improve these water
qualities for the purpose of water reuse, working well with secondary or tertiary treated water as
shown in Figure 1 of ISO 20468-1:2018 and in Annex A.
In this guideline, the dedicated features to ozone technology for water reuse are described and the
requirements for proper and accurate evaluation of ozone system for water reuse are offered.
© ISO 2020 – All rights reserved v

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INTERNATIONAL STANDARD ISO 20468-3:2020(E)
Guidelines for performance evaluation of treatment
technologies for water reuse systems —
Part 3:
Ozone treatment technology
1 Scope
This document specifies performance evaluation methods of treatment technology using ozone for
water reuse systems. It deals with how to measure typical parameters which indicate performance of
ozone treatment technology.
2 Normative references
The following documents are referred to in the text in such a way that some or all of their content
constitutes requirements of this document. For dated references, only the edition cited applies. For
undated references, the latest edition of the referenced document (including any amendments) applies.
ISO 20670, Water reuse — Vocabulary
3 Terms, definitions and abbreviated terms
For the purposes of this document, the following terms and definitions given in ISO 20670 and the
following apply.
ISO and IEC maintain terminological databases for use in standardization at the following addresses:
— ISO Online browsing platform: available at https:// www .iso .org/ obp
— IEC Electropedia: available at http:// www .electropedia .org/
3.1 Terms and definitions
3.1.1
ambient ozone concentration
concentration of ozone existing in the air or surrounding the ozone treatment apparatus
3.1.2
exhaust residual ozone concentration
ozone concentration (3.1.6) at the outlet of an off-gas ozone treatment unit
3.1.3
generated ozone amount
mass of ozone generated in a unit time
3.1.4
generated ozone concentration
ozone concentration (3.1.6) in the gas phase at the outlet of an ozone generator
3.1.5
off-gas ozone concentration
ozone concentration at the outlet of an ozone contactor
© ISO 2020 – All rights reserved 1

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ISO 20468-3:2020(E)

3.1.6
ozone concentration
volume, mass or mole of ozone in a unit volume or mass of gas or liquid
3.1.7
ozone concentration monitor
instrument capable of measuring ozone concentration in samples continuously
3.1.8
ozone demand
amount of ozone consumed to oxidize material in water
3.1.9
ozone dose
mass of ozone injected into a unit volume of water
3
Note 1 to entry: Ozone dose is expressed in units of mass-per-volume concentration (g/m or mg/l).
3.1.10
residual ozone concentration
dissolved ozone concentration measured after a given contact time
Note 1 to entry: It is expressed in mg/l.
3.1.11
transferred ozone dose
mass of ozone applied into a unit volume of water
3
Note 1 to entry: Transferred ozone dose is expressed in units of mass-per-volume concentration (g/m or mg/l).
3.2 Abbreviated terms
CT product of residual concentration and time
EPDM ethylene propylene diene monomer
FRP fiber-reinforced plastic
GHG greenhouse gases
LOX liquid oxygen
LRVs log-reduction values
PTFE polytetrafluoroethylene
SS stainless steel
UV ultraviolet
4 System configuration
4.1 General
The ozone system for water treatment consists of:
— a feed gas supply unit
— an ozone generation unit
2 © ISO 2020 – All rights reserved

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ISO 20468-3:2020(E)

— an ozone contact unit
— an off-gas ozone treatment unit
Depending on the water treatment efficiency and performance to be achieved, pre-treatment and/
or post-treatment can be added to the ozone system. For example, sand filtration as the typical pre-
treatment process to remove suspended impurities including ozone scavengers and inorganic matter
enhances treated water quality and reduces ineffective ozone consumption. On the other hand, post-
treatment such as biological activated carbon process removes residual particles and dissolved matter
which are not decomposed and/or are generated as by-products during ozonation. In order to retain
bactericidal effects after ozonation, post disinfection such as chlorine disinfection can be added.
4.2 Ozone system for water treatment
4.2.1 Feed gas supply unit
The feed gas supply unit is using either air or oxygen gas to the ozone generation unit. An air-fed ozone
system uses compressed air directly from the atmosphere. An oxygen-fed ozone system uses LOX
or concentrated oxygen fed by an oxygen concentrator. Typically, the oxygen concentrator increases
oxygen concentration by adsorbing nitrogen selectively from air.
4.2.2 Ozone generation unit
The ozone generation unit typically consists of:
— ozone generator(s)
— a power supply
— a cooling system
Corona discharge is currently the most common ozone generation method.
4.2.3 Ozone contact unit
The ozone contact unit typically consists of:
— an ozone dissolution system
— ozone contactor(s)
The ozone contactor is a vessel where ozone is dissolved in water and reacts with target substance(s),
followed by the ozone dissolution system which dissolves ozone gas in water. Mass transfer of ozone
is a critical aspect of water ozonation. Dissolution devices include bubble diffusion, down flow tube
injection, venturi injection, radial diffuser, static mixers and mechanical agitation. These applicable
dissolution devices should be selected depending on the space limitation for system installation, electric
power charge and ozone transfer efficiency. The method of ozone gas dissolution used also depends on
system design and method of ozone generation used.
4.2.4 Off-gas ozone treatment unit
Since ozone is a very strong oxidant, any unreacted ozone in the off-gas can be harmful to the
environment and endanger human health. Consequently, it shall be converted to oxygen and neutralized
before the off-gas is released to atmosphere.
The off-gas ozone treatment unit typically consists of an off-gas ozone destruction unit and an off-gas
ozone suction unit. The off-gas ozone suction unit withdraws off-gas ozone from the ozone contactor
and draws it into the off-gas ozone destruction unit. The off-gas ozone destruction unit converts ozone
residual exhausted from the ozone contactor to oxygen by using such methods as activated carbon,
catalyst media and heat, or combination of heat and catalyst media.
© ISO 2020 – All rights reserved 3

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ISO 20468-3:2020(E)

4.2.5 Ozone measuring system
Various types of ozone monitors are available for measuring ozone concentrations. The typical
configuration of ozone treatment system as well as the monitoring points of ozone concentration are
shown in Figure 1.
Figure 1 — Typical configuration of ozonation system and ozone concentration monitoring points
The high concentration ozone monitor, residual ozone concentration monitor and off-gas ozone
concentration monitor are installed to measure ozone concentration at key locations in the ozonation
system for the purpose of controlling ozone generation and dose. Specific descriptions about ozone
generation control methods are shown in Annex D.
The exhaust and ambient ozone monitors measure ozone concentrations to verify safe operating
conditions. The control system works automatically for system shutdown or stopping ozone production
if necessary.
5 Principles and general guidelines for performance evaluation
5.1 General
Based on the principles and general guidelines for performance verification described in
[1]
ISO 20468-1:2018 , this document also specifies two kinds of performance requirements:
— functional requirements
— non-functional requirements
5.2 Functional requirements
5.2.1 General
Functional requirements consist of two parts; water quality based performance and process-based
performance, both of which strongly influence the conformity of produced water quality to water reuse
regulations and related standards.
4 © ISO 2020 – All rights reserved

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ISO 20468-3:2020(E)

Water quality based performance for ozone treatment includes the potential reduction of disease causing
microorganisms that can be present and the removal of specific constituents such as colour and odour
(Annex A). They are generally expressed as a logarithmic-scale reduction and a residual constituent
concentration in the treated reuse water, respectively. On the other hand, ultra-violet absorbance and
ultra-violet transmission can be used as surrogate indicators to check the removal efficacy of dissolved
organic carbon. These water quality parameters and indicators should be in accordance with the water
reuse regulations and standards stipulated in respective countries (examples in Annex B).
The reduction in, or residual concentration of, Escherichia coli, enterococci bacteria, thermo-tolerant
coliform bacteria and total coliform bacteria can be used as potential indicators of microorganisms
to assess the effectiveness of ozone disinfection in reducing pathogenic microorganisms that can be
present in the source water. Quantification of these microbial indicators can be carried out by using
[2]
analysis methods stipulated in ISO 6222:1999 .
The reduction of concentration in pharmaceutical and personal care products and other contaminants
of emerging concern, as well as colour and odour, can also be functional requirements for some reuse
applications. Colour and odour can be quantified by the methods stipulated in Standard Methods for
[3]
the Examination of Water and Wastewater . The analytical methods and water quality parameters
should be required by the regulations in respective countries.
The CT approach could be used for wastewater ozonation but is much less relevant than in drinking
water. It is noted that a sufficient ozone dose to achieve the targeted water quality should be transferred
to the effluent resulting in detection of residual ozone concentration.
Ideally, supplied ozone should be used completely in the reactor. However, if the off-gas ozone
concentration indicates zero, it is practically impossible to correctly estimate transferred ozone dose.
Therefore, the concentration of off-gas ozone before the destruction should be as low as possible by
providing just enough amount of ozone for treatment.
On the other hand, process-based performance for ozone treatment is concerned with the functional
performance of main units of ozone treatment system such as ozone generators and contactors and is
assessed by monitoring the ozone concentration in different points (Annex C and D). The dependability
of these units is also important as a part of process-based performance since failure in ozone generators
and/or contactors can lead to releasing insufficient transferred ozone into water.
Failure in off-gas ozone treatment units can raise an issue of undestroyed ozone gas leaking to rooms,
with the possibility of personnel injury and/or property damage in the worst-case situation. Therefore,
the dependability of off-gas ozone treatment units should be included into non-functional requirements.
5.2.2 Performance evaluation procedures
5.2.2.1 STEP1 — Setting performance criteria and objectives
An ozone treatment system is expected to improve water quality parameters such as E. coli, thermo-
tolerant coliforms, colour and odour. The water quality standards for these parameters as water-quality
based performance criteria should be set for the purpose of water reuse.
Those reuse water quality parameters are standardized in some countries for landscape, amenity and
other purposes, as illustrated in Annex B.
The values of the reclaimed water quality parameters should be some of the values that presented in
[4]
Annex A of ISO 20761:2018 .
In addition, to ensure the functionality and reliability of water reclamation processes for pathogen
control in the case of high risk of exposure, the health risk management strategy can also include
targets for log-reduction values (LRVs). Other water quality parameters can be relevant for specific
non-potable water applications, such as those described in ISO 16075-1, ISO 16075-2, ISO 16075-3:2015,
[5]
ISO 16075-4:2016 for irrigation. Further information on the risk assessment and management
[6]
approach can be found in ISO 20426:2018 , ISO 20761:2018 and in Australian Guidelines for Water
[7]
Recycling .
© ISO 2020 – All rights reserved 5

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ISO 20468-3:2020(E)

On the other hand, in order to meet the target water quality consistently, the ozone system is required
to be operated properly. From this viewpoint, the parameters of operational conditions should be
included into process-based performance indicators.
5.2.2.2 STEP 2 — Performance evaluation
Water quality based performance of ozone treatment system for water reuse can be evaluated by
periodically measuring residual concentrations of the target constituents. The residual concentrations
should be assessed frequently enough to ensure operating parameters and regulatory and aesthetic
reuse water quality objectives are consistently met. The monitoring program and sampling frequency
should be in accordance with the standards in respective countries.
At the same time, it is important to measure the ozone concentration. Figure 1 shows the typical
configuration of ozone treatment system as well as monitoring points of ozone concentration as
operating conditions; ozone concentration at M1 and M3 points should be monitored as shown in
Annex C to effectively evaluate the treatment system performance. When those concentrations meet
the target values, it is confirmed that the appropriate amount of ozone is supplied and consumed in the
ozone contactor to achieve the functional requirement on water quality.
Furthermore, the following parameters are also expected to function well as process-based
performance indicators:
a) Generated ozone amount
Generated ozone amount is calculated by the following formula.
     (Generated ozone amount) = (Generated ozone concentration) × (Ozone gas flow rate)
The value of generated ozone amount should be larger than ozone demand.
b) Ozone dose
Ozone dose is calculated by ozone gas flow rate, water flow rate and generated ozone concentration.
     (Ozone dose) = (Ozone gas flow rate) × (Generated ozone concentration) / (Water flow rate)
Ozone dose should be controlled to provide sufficient amount of ozone to achieve targeted water
quality.
c) Transferred Ozone dose
Transferred ozone dose is calculated by ozone gas flow rate, water flow rate, generated ozone
concentration and off-gas ozone concentration.
     (Transferred ozone dose) = (Ozone gas flow rate) × (Generated ozone concentration – Off-gas
      ozone concentration) / (Water flow rate)
In case that off-gas ozone concentration is sufficiently low, ozone dose would be equal to transferred
ozone dose.
d) Mass transfer efficiency
Mass transfer efficiency shows how much ozone is transferred into water out of generated
ozone amount. Specifically, it is calculated by generated ozone concentration and off-gas ozone
concentration.
     (Mass transfer efficiency) = (Generated ozone concentration – Off-gas ozone concentration) /
     (Generated ozone concentration) × 100
This value is normally between 80 to less than 100 %, depending on dissolution methods.
6 © ISO 2020 – All rights reserved

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ISO 20468-3:2020(E)

5.2.2.3 STEP 3 — Diagnosis of causes for unsatisfactory performance
If one or more operating objectives or water quality requirements are not being attained, the ozone
system may be malfunctioning, and corrective measures are required. Possible failures may be
decreased ozone generation or degradation of mass transfer efficiency:
a) Decrease in ozone generation
— check whether ozone concentration monitor (M1) works properly.
— check feed gas quality (Oxygen purity, dew point) and flow rate.
— check the ozone generator and/or the control panel whether any error messages are indicated.
b) Degradation of mass transfer efficiency
— check damage on diffusers (in case of diffusers used).
— check failure on a booster pump (in case of injectors used).
— check damage on injectors or static mixers (in case of injectors used).
— check whether the ratio of gas flow rate to water flow rate is being maintained within the
required range of ratio depending on the dissolution devices.
In the case that no failures are found on ozone generation and mass transfer efficiency:
— check the water quality and quantity under treatment and adjust the ozone supply to satisfy the
ozone demand.
— check upstream secondary and tertiary treatments to improve the water quality prior to ozonation
to satisfy the design bases.
5.3 Non-functional requirements
5.3.1 Performance characteristics
The following two performance characteristics are provided.
a) Environmental and economic key factors (5.3.2)
b) Safety requirements (5.3.3)
5.3.2 Environmental and economic key factors
Environmental and economic factors for an ozonation system include:
— Electric power consumption for oxygen and ozone generation.
— Electric power consumption for ozone transfer, if needed.
— Electric power consumption for the off-gas ozone destruction/treatment uni
...

FINAL
INTERNATIONAL ISO/FDIS
DRAFT
STANDARD 20468-3
ISO/TC 282/SC 3
Guidelines for performance evaluation
Secretariat: JISC
of treatment technologies for water
Voting begins on:
2020-03-03 reuse systems —
Voting terminates on:
Part 3:
2020-04-28
Ozone treatment technology
RECIPIENTS OF THIS DRAFT ARE INVITED TO
SUBMIT, WITH THEIR COMMENTS, NOTIFICATION
OF ANY RELEVANT PATENT RIGHTS OF WHICH
THEY ARE AWARE AND TO PROVIDE SUPPOR TING
DOCUMENTATION.
IN ADDITION TO THEIR EVALUATION AS
Reference number
BEING ACCEPTABLE FOR INDUSTRIAL, TECHNO-
ISO/FDIS 20468-3:2020(E)
LOGICAL, COMMERCIAL AND USER PURPOSES,
DRAFT INTERNATIONAL STANDARDS MAY ON
OCCASION HAVE TO BE CONSIDERED IN THE
LIGHT OF THEIR POTENTIAL TO BECOME STAN-
DARDS TO WHICH REFERENCE MAY BE MADE IN
©
NATIONAL REGULATIONS. ISO 2020

---------------------- Page: 1 ----------------------
ISO/FDIS 20468-3:2020(E)

COPYRIGHT PROTECTED DOCUMENT
© ISO 2020
All rights reserved. Unless otherwise specified, or required in the context of its implementation, no part of this publication may
be reproduced or utilized otherwise in any form or by any means, electronic or mechanical, including photocopying, or posting
on the internet or an intranet, without prior written permission. Permission can be requested from either ISO at the address
below or ISO’s member body in the country of the requester.
ISO copyright office
CP 401 • Ch. de Blandonnet 8
CH-1214 Vernier, Geneva
Phone: +41 22 749 01 11
Fax: +41 22 749 09 47
Email: copyright@iso.org
Website: www.iso.org
Published in Switzerland
ii © ISO 2020 – All rights reserved

---------------------- Page: 2 ----------------------
ISO/FDIS 20468-3:2020(E)

Contents Page
Foreword .iv
Introduction .v
1 Scope . 1
2 Normative references . 1
3 Terms, definitions and abbreviated terms . 1
3.1 Terms and definitions . 1
3.2 Abbreviated terms . 2
4 System configuration . 2
4.1 General . 2
4.2 Ozone system for water treatment . 3
4.2.1 Feed gas supply unit. 3
4.2.2 Ozone generation unit . 3
4.2.3 Ozone contact unit . . 3
4.2.4 Off-gas ozone treatment unit . 3
4.2.5 Ozone measuring system . 4
5 Principles and general guidelines for performance evaluation . 4
5.1 General . 4
5.2 Functional requirements . 4
5.2.1 General. 4
5.2.2 Performance evaluation procedures . 5
5.3 Non-functional requirements . 7
5.3.1 Performance characteristics . 7
5.3.2 Environmental and economic key factors . 7
5.3.3 Safety requirements . 8
Annex A (informative) Main treatment technologies and target constituents for water reuse .9
Annex B (informative) Reuse water quality parameters .10
Annex C (informative) Ozone concentration monitoring points .23
Annex D (informative) Ozone generation control methods .25
Bibliography .26
© ISO 2020 – All rights reserved iii

---------------------- Page: 3 ----------------------
ISO/FDIS 20468-3:2020(E)

Foreword
ISO (the International Organization for Standardization) is a worldwide federation of national standards
bodies (ISO member bodies). The work of preparing International Standards is normally carried out
through ISO technical committees. Each member body interested in a subject for which a technical
committee has been established has the right to be represented on that committee. International
organizations, governmental and non-governmental, in liaison with ISO, also take part in the work.
ISO collaborates closely with the International Electrotechnical Commission (IEC) on all matters of
electrotechnical standardization.
The procedures used to develop this document and those intended for its further maintenance are
described in the ISO/IEC Directives, Part 1. In particular, the different approval criteria needed for the
different types of ISO documents should be noted. This document was drafted in accordance with the
editorial rules of the ISO/IEC Directives, Part 2 (see www .iso .org/ directives).
Attention is drawn to the possibility that some of the elements of this document may be the subject of
patent rights. ISO shall not be held responsible for identifying any or all such patent rights. Details of
any patent rights identified during the development of the document will be in the Introduction and/or
on the ISO list of patent declarations received (see www .iso .org/ patents).
Any trade name used in this document is information given for the convenience of users and does not
constitute an endorsement.
For an explanation of the voluntary nature of standards, the meaning of ISO specific terms and
expressions related to conformity assessment, as well as information about ISO's adherence to the
World Trade Organization (WTO) principles in the Technical Barriers to Trade (TBT) see www .iso .org/
iso/ foreword .html.
This document was prepared by Technical Committee ISO/TC 282, Water reuse, Subcommittee SC 3,
Risk and performance evaluation of water reuse system.
Any feedback or questions on this document should be directed to the user’s national standards body. A
complete listing of these bodies can be found at www .iso .org/ members .html.
iv © ISO 2020 – All rights reserved

---------------------- Page: 4 ----------------------
ISO/FDIS 20468-3:2020(E)

Introduction
The rapidly growing global market for water reuse technologies inevitably demands standards which
are applicable on a world-wide basis. Many regions in the world are facing water shortages, and there is
great interest in the use of technologies that can treat wastewater and make the reuse water available
for a wide range of reuse applications that can satisfy non-potable water demands, thereby conserving
precious potable water supplies. Simultaneously, the implementation of water reuse schemes is raising
public and regulatory concerns regarding potential human health, environmental and societal impacts.
This has led to an increasing need to specify various aspects of water reuse projects and there is a
growing need on behalf of regulators, reuse technology suppliers, and users of those technologies for
international standardization. Without ISO water reuse standards, a great number of opportunities for
sustainable development based on water reuse will be lost.
Standardization needs to include objective specification and evaluation of levels of service and water
reuse system performance dependability, including safety, environmental protection, and resilience and
cost-effectiveness considerations. Hence, appropriate methods are needed to evaluate the performance
of water reuse systems.
The performance of treatment technologies for water reuse, inter alia, should be evaluated properly in
order to select the most appropriate technologies in an unbiased way to achieve the objectives of the
water reuse project. Despite considerable research and development on treatment technologies, such
scientific knowledge is largely held within commercial interests. Given less than ideal communication
between producers and users of reuse technologies with regards to treatment performance, clear
information as to what to measure on the one hand and what level of performance is required on the
other is currently missing. To address these challenges, this document provides methods and tools,
which can be accepted by most stakeholders, to evaluate the performance of treatment technologies for
water reuse systems from multitude of applications.
Based on the discussion in the meetings of ISO/TC 282/SC 3, ISO 20468-1 titled “Guidelines for
performance evaluation of treatment technologies for water reuse systems — Part 1: General” has been
developed to establish the standard of generic aspects for performance evaluation. In this context,
this document stipulating specific ways of performance evaluation of ozone treatment technology,
commonly known as ozonation, for water reuse systems, based on ISO 20468-1 as the generic standard,
is established herein.
Ozone (O ) is an allotrope of oxygen (O ) and is the second strongest oxidiser after fluorine. Its strong
3 2
oxidative decomposition power makes it effective as a disinfectant and in removal of oxidizable
constituents in water. There are cases where ozonation at high doses is used to remove micro-pollutants
in wastewater for environmental protection.
In various types of water reuse systems, the disinfection and the removal of colour and odour are
essential. Then it can be said that ozone technology plays an important role to improve these water
qualities for the purpose of water reuse, working well with secondary or tertiary treated water as
shown in Figure 1 of ISO 20468-1:2018 and in Annex A.
In this guideline, the dedicated features to ozone technology for water reuse are instructed and the
requirements for proper and accurate evaluation of ozone system for water reuse are offered.
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FINAL DRAFT INTERNATIONAL STANDARD ISO/FDIS 20468-3:2020(E)
Guidelines for performance evaluation of treatment
technologies for water reuse systems —
Part 3:
Ozone treatment technology
1 Scope
This document specifies performance evaluation methods of treatment technology using ozone for
water reuse systems. It deals with how to measure typical parameters which indicate performance of
ozone treatment technology.
2 Normative references
The following documents are referred to in the text in such a way that some or all of their content
constitutes requirements of this document. For dated references, only the edition cited applies. For
undated references, the latest edition of the referenced document (including any amendments) applies.
ISO 20670, Water reuse — Vocabulary
3 Terms, definitions and abbreviated terms
For the purposes of this document, the following terms and definitions given in ISO 20670 and the
following apply.
ISO and IEC maintain terminological databases for use in standardization at the following addresses:
— ISO Online browsing platform: available at https:// www .iso .org/ obp
— IEC Electropedia: available at http:// www .electropedia .org/
3.1 Terms and definitions
3.1.1
ambient ozone concentration
concentration of ozone existing in the air or surrounding the ozone treatment apparatus
3.1.2
exhaust residual ozone concentration
ozone concentration at the outlet of an off-gas ozone treatment unit
3.1.3
generated ozone amount
quantity of ozone generated in a unit time
3.1.4
generated ozone concentration
ozone concentration in the gas phase at the outlet of an ozone generator
3.1.5
off-gas ozone concentration
ozone concentration at the outlet of an ozone contactor
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3.1.6
ozone concentration
volume, mass or mole of ozone in a unit volume or mass of gas or liquid
3.1.7
ozone concentration monitor
instrument capable of measuring ozone concentration in samples continuously
3.1.8
ozone demand
amount of ozone consumed to oxidize material in water
3.1.9
ozone dose
mass of ozone injected into a unit volume of water
3
Note 1 to entry: Ozone dose is expressed in units of mass-per-volume concentration (g/m or mg/l).
3.1.10
residual ozone concentration
dissolved ozone concentration measured after a given contact time
Note 1 to entry: It is expressed in mg/l.
3.1.11
transferred ozone dose
mass of ozone applied into a unit volume of water
3
Note 1 to entry: Transferred ozone dose is expressed in units of mass-per-volume concentration (g/m or mg/l).
3.2 Abbreviated terms
CT product of residual concentration and time
EPDM ethylene propylene diene monomer
FRP fiber-reinforced plastic
GHG greenhouse gases
LOX liquid oxygen
LRVs log-reduction values
PTFE polytetrafluoroethylene
4 System configuration
4.1 General
The ozone system for water treatment consists of:
— a feed gas supply unit
— an ozone generation unit
— an ozone contact unit
— an off-gas ozone treatment unit
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Depending on the water treatment efficiency and performance to be achieved, pre-treatment and/
or post-treatment can be added to the ozone system. For example, sand filtration as the typical pre-
treatment process to remove suspended impurities including ozone scavengers and inorganic matter
enhances treated water quality and reduces ineffective ozone consumption. On the other hand, post-
treatment such as biological activated carbon process removes residual particles and dissolved matter
which are not decomposed and/or are generated as by-products during ozonation. In order to retain
bactericidal effects after ozonation, post disinfection such as chlorine disinfection can be added.
4.2 Ozone system for water treatment
4.2.1 Feed gas supply unit
The feed gas supply unit is using either air or oxygen gas to the ozone generation unit. An air-fed ozone
system uses compressed air directly from the atmosphere. An oxygen-fed ozone system uses LOX
or concentrated oxygen fed by an oxygen concentrator. Typically, the oxygen concentrator increases
oxygen concentration by absorbing nitrogen selectively from air.
4.2.2 Ozone generation unit
The ozone generation unit typically consists of:
— ozone generator(s)
— a power supply
— a cooling system
Corona discharge is currently the most common ozone generation method.
4.2.3 Ozone contact unit
The ozone contact unit typically consists of:
— an ozone dissolution system
— ozone contactor(s)
The ozone contactor is a vessel where ozone is dissolved in water and reacts with target substance(s),
followed by the ozone dissolution system which dissolves ozone gas in water. Mass transfer of ozone
is a critical aspect of water ozonation. Dissolution devices include bubble diffusion, down flow tube
injection, venturi injection, radial diffuser, static mixers and mechanical agitation. These applicable
dissolution devices should be selected depending on the space limitation for system installation, electric
power charge and so on. The method of ozone gas dissolution used also depends on system design and
method of ozone generation used.
4.2.4 Off-gas ozone treatment unit
Since ozone is a very strong oxidant, any unreacted ozone in the off-gas can be harmful to the
environment and endanger human health. Consequently, it shall be converted to oxygen and neutralized
before the off-gas is released to atmosphere.
The off-gas ozone treatment unit typically consists of an off-gas ozone destruction unit and an off-gas
ozone suction unit. The off-gas ozone suction unit withdraws off-gas ozone from the ozone contactor
and draws it into the off-gas ozone destruction unit. The off-gas ozone destruction unit converts ozone
residual exhausted from the ozone contactor to oxygen by using such methods as activated carbon,
catalyst media and heat, or combination of heat and catalyst media.
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4.2.5 Ozone measuring system
Various types of ozone monitors are available for measuring ozone concentrations. The typical
configuration of ozone treatment system as well as the monitoring points of ozone concentration are
shown in Figure 1.
Figure 1 — Typical configuration of ozonation system and ozone concentration monitoring points
The high concentration ozone monitor, residual ozone concentration monitor and off-gas ozone
concentration monitor are installed to measure ozone concentration at key locations in the ozonation
system for the purpose of controlling ozone generation and dose. Specific descriptions about ozone
generation control methods are shown in Annex D.
The exhaust and ambient ozone monitors measure ozone concentrations to verify safe operating
conditions. The control system works automatically for system shutdown or stopping ozone production
if needed.
5 Principles and general guidelines for performance evaluation
5.1 General
Based on the principles and general guidelines for performance verification described in
[1]
ISO 20468-1:2018 , this document also specifies two kinds of performance requirements:
— functional requirements
— non-functional requirements
5.2 Functional requirements
5.2.1 General
Functional requirements consist of two parts; water quality based performance and process-based
performance, both of which strongly influence the conformity of produced water quality to water reuse
regulations and related standards.
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Water quality based performance for ozone treatment includes the potential reduction of disease causing
microorganisms that can be present and the removal of specific constituents such as colour and odour
(Annex A). They are generally expressed as a logarithmic-scale reduction and a residual constituent
concentration in the treated reuse water, respectively. On the other hand, ultra-violet absorbance and
ultra-violet transmission can be used as surrogate indicators to check the removal efficacy of dissolved
organic carbon. These water quality parameters and indicators should be in accordance with the water
reuse regulations and standards stipulated in respective countries (examples in Annex B).
The reduction in, or residual concentration of, Escherichia coli, enterococci bacteria, thermo-tolerant
coliform bacteria and total coliform bacteria can be used as potential indicators of microorganisms
to assess the effectiveness of ozone disinfection in reducing pathogenic microorganisms that can be
present in the source water. Quantification of these microbial indicators can be carried out by using
[2]
analysis methods stipulated in ISO 6222:1999 .
The reduction of concentration in pharmaceutical and personal care products and other contaminants
of emerging concern, as well as colour and odour, can also be functional requirements for some reuse
applications. Colour and odour can be quantified by the methods stipulated in Standard Methods for
[3]
the Examination of Water and Wastewater . The analytical methods and water quality parameters
should be required by the regulations in respective countries.
The CT approach could be used for wastewater ozonation but is much less relevant than in drinking
water. It is noted that a sufficient ozone dose to achieve the targeted water quality should be transferred
to the effluent resulting in detection of residual ozone concentration.
Ideally, supplied ozone should be used completely in the reactor. However, if the off-gas ozone
concentration indicates zero, it is practically impossible to correctly estimate transferred ozone dose.
Therefore, the concentration of off-gas ozone before the destruction should be as low as possible by
providing just enough amount of ozone for treatment.
On the other hand, process-based performance for ozone treatment is concerned with the functional
performance of main units of ozone treatment system such as ozone generators and contactors and is
assessed by monitoring the ozone concentration in different points (Annex C and D). The dependability
of these units is also important as a part of process-based performance since failure in ozone generators
and/or contactors can lead to releasing insufficient transferred ozone into water.
Failure in off-gas ozone treatment units can raise an issue of undestroyed ozone gas leaking to rooms,
with the possibility of personnel injury and/or property damage in the worst-case situation. Then the
dependability of off-gas ozone treatment units should be included into non-functional requirements.
5.2.2 Performance evaluation procedures
5.2.2.1 STEP1 — Setting performance criteria and objectives
An ozone treatment system is expected to improve water quality parameters such as E. coli, thermo-
tolerant coliforms, colour and odour. The water quality standards for these parameters as water-quality
based performance criteria should be set for the purpose of water reuse.
Those reuse water quality parameters are standardized in some countries for landscape, amenity and
other purposes, as illustrated in Annex B.
The values of the reclaimed water quality parameters should be some of the values that presented in
[4]
Annex A of ISO 20761:2018 .
In addition, to ensure the functionality and reliability of water reclamation processes for pathogen
control in the case of high risk of exposure, the health risk management strategy can also include
targets for log-reduction values (LRVs). Other water quality parameters can be relevant for specific
non-potable water applications, such as those described in ISO 16075-1, ISO 16075-2, ISO 16075-3:2015,
[5]
ISO 16075-4:2016 for irrigation. Further information on the risk assessment and management
[6]
approach can be found in ISO 20426:2018 , ISO 20761:2018 and in Australian Guidelines for Water
[7]
Recycling .
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On the other hand, in order to meet the target water quality constantly, the ozone system is required to
be operated properly. From this viewpoint, the parameters of operational conditions should be included
into process-based performance indicators.
5.2.2.2 STEP 2 — Performance evaluation
Water quality based performance of ozone treatment system for water reuse can be evaluated by
periodically measuring residual concentrations of the target constituents. The residual concentrations
should be assessed frequently enough to ensure operating parameters and regulatory and aesthetic
reuse water quality objectives are consistently met. The monitoring program and sampling frequency
should be in accordance with the standards in respective countries.
At the same time, it is important to measure the ozone concentration. Figure 1 shows the typical
configuration of ozone treatment system as well as monitoring points of ozone concentration as
operating conditions; ozone concentration at M1 and M3 points should be monitored as shown in
Annex C to conveniently evaluate the treatment system performance. When those concentrations meet
the target values, it is confirmed that the appropriate amount of ozone is supplied and consumed in the
ozone contactor to achieve the functional requirement on water quality.
Furthermore, the following parameters are also expected to function well as process-based
performance indicators:
a) Generated ozone amount
Generated ozone amount is calculated by the following formula.
     (Generated ozone amount) = (Generated ozone concentration) × (Ozone gas flow rate)
The value of generated ozone amount should be larger than ozone demand.
b) Ozone dose
Ozone dose is calculated by ozone gas flow rate, water flow rate and generated ozone concentration.
     (Ozone dose) = (Ozone gas flow rate) × (Generated ozone concentration) / (Water flow rate)
Ozone dose should be controlled to provide sufficient amount of ozone to achieve targeted water
quality.
c) Transferred Ozone dose
Transferred ozone dose is calculated by ozone gas flow rate, water flow rate, generated ozone
concentration and off-gas ozone concentration.
     (Transferred ozone dose) = (Ozone gas flow rate) × (Generated ozone concentration – Off-gas
      ozone concentration) / (Water flow rate)
In case that off-gas ozone concentration is sufficiently low, ozone dose would be equal to transferred
ozone dose.
d) Mass transfer efficiency
Mass transfer efficiency shows how much ozone is transferred into water out of generated ozone
amount. Specifically, it is calculated by ozone gas flow rate, generated ozone concentration and off-
gas ozone concentration.
     (Mass transfer efficiency) = (Generated ozone concentration) – (Off-gas ozone concentration) /
     (Generated ozone concentration)
This value is normally between 80 to less than 100 %, depending on dissolution methods.
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5.2.2.3 STEP 3 — Diagnosis of causes for unsatisfactory performance
If one or more operating objectives or water quality requirements are not being attained, the ozone
system may be malfunctioning and corrective measures are required. Possible failures may be the
ozone generation decrease or degradation of mass transfer efficiency:
a) Decrease in ozone generation
— check whether ozone concentration monitor (M1) works properly.
— check feed gas quality (Oxygen purity, dew point) and flow rate.
— check the ozone generator and/or the control panel whether any error messages are indicated.
b) Degradation of mass transfer efficiency
— check damage on diffusers (in case of diffusers used).
— check failure on a booster pump (in case of injectors used).
— check damage on injectors or static mixers (in case of injectors used).
— check whether the ratio of gas flow rate to water flow rate remains in adequacy with the
required range of ratio depending on the dissolution devices.
In the case that no failures are found on ozone generation and mass transfer efficiency:
— check the water quality and quantity under treatment and adjust the ozone supply to satisfy the
ozone demand.
— check earlier secondary and tertiary treatments to improve the water quality prior to ozonation to
satisfy the designed value.
5.3 Non-functional requirements
5.3.1 Performance characteristics
The following two performance characteristics are provided.
a) Environmental and economic
...

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