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Sludge Ozonation<br />
Tokyo, Site of Upcoming <strong>Ozone</strong> World Congress<br />
OZONE NEWS Volume 37, No. 3 • June, 20<strong>09</strong><br />
!
<strong>Ozone</strong> News Volume 37, No.3<br />
OZONE NEWS<br />
Volume 37, No. 3 June, 20<strong>09</strong><br />
Editor: Barry L. Loeb<br />
<strong>Ozone</strong> News (ISSN 1065-5905) is a bimonthly publication of the <strong>International</strong><br />
<strong>Ozone</strong> Association (IOA). Annual Subscription Rate $150.00. For editorial and<br />
advertising information, please contact:<br />
<strong>International</strong> <strong>Ozone</strong> Association/Editorial Office<br />
9731 Pebble View Drive<br />
Cincinnati, Ohio 45252-2167<br />
Tel./ Fax: (1) 513.385.3906<br />
Email: blloeb@fuse.net<br />
Membership and Publication Information:<br />
The <strong>International</strong> <strong>Ozone</strong> Association is a nonprofit educational and scientific<br />
organization dedicated to the collection and dissemination of information on,<br />
and to promote research in, any and all aspects of ozone and related oxygen<br />
species technologies. Membership is open to any individual, corporation, or<br />
organization having interest in the latest developments and advancements in<br />
ozone technology.<br />
As a member of the IOA, you will receive bimonthly issues of the <strong>Ozone</strong> News<br />
newsletter, bimonthly issues of the technical journal <strong>Ozone</strong>: Science &<br />
Engineering (OS&E), and IOA's Publication Catalog which includes<br />
worldwide conference proceedings, monographs, and special reprints. In<br />
addition, members receive discounts on IOA worldwide publications and<br />
meetings.<br />
Website: www.io3a.org<br />
For membership and publication information, please contact the IOA office<br />
nearest you:<br />
Pan American Group (PAG)<br />
Mr. Paul Overbeck, Executive Director<br />
<strong>International</strong> <strong>Ozone</strong> Association, Pan American Group<br />
PO Box 28873, Scottsdale, AZ 85255<br />
Tel: (1)480-529-3787<br />
Fax: (1)480-473-9068<br />
Email: info@io3a.org; pauloverbeck@io3a.org<br />
European-African-Asian-Australasian Group (EA3G)<br />
Mr. François Mauvais, SecretaryTreasurer<br />
Association <strong>International</strong>e de l'<strong>Ozone</strong><br />
83 avenue Foch F-75116 Paris, France<br />
Tel: 33 (0) 1 53 70 13 56<br />
Fax: 33 (0) 1 53 70 13 40<br />
Email: francois.mauvais@astee.org<br />
Ms. Beatrice Bernard, Secretariat<br />
IOA-EA3G -ESIP-Plate-Forme Eaux, 40 av. du Recteur Pineau<br />
86022 Poitiers Cedex, France<br />
Tel: 33 (0) 5 49 45 44 54<br />
Fax: 33 (0) 5 49 45 40 60<br />
Email: ioa@esip.univ-poitiers.fr; Web: www.ioa-ea3g.org<br />
Nippon Islands Group (NIG)<br />
Mr. Hirofumi Takahara<br />
<strong>International</strong> <strong>Ozone</strong> Association<br />
#301, 10-10 Nihonbashi Omizawacho<br />
Chuo-ku, Tokyo 103-0006, Japan<br />
Tel: (81) 3 6661 1622<br />
Fax: (81) 3 6661 1623<br />
Email:takahara-joa@mrh.biglobe.ne.jp web: www.j-ozone.org<br />
Page 3<br />
INSIDE THIS ISSUE<br />
-bbbbbbb<br />
ON TTHE<br />
COVER<br />
<strong>Ozone</strong> for Sludge Concentration; Tokyo<br />
World Congress. Stories on pp. 15 &<br />
26.<br />
4 Index of Advertisers<br />
5 Editor’s Notes<br />
6 INDUSTRY NEWS<br />
- Emerging Contaminant Study<br />
- Reference Document - Best Available<br />
Technologies<br />
8 - Mazzei Pipeline Flash Reactor<br />
9 - Trojan Technologies forms VIQUA<br />
- ENMET Introduces Carbon Dioxide<br />
Sensor<br />
12 - Report from Boston Conference<br />
15 -Full Scale Application of a Novel<br />
Sludge Ozonation Process<br />
21 New IOA Members<br />
23 Meetings Calendar<br />
25 Announcement of Cuba Conference<br />
26 Tokyo World Congress Preliminary<br />
Program
<strong>Ozone</strong> News Volume 37, No 3<br />
Registration Open for Tokyo World<br />
Congress<br />
Registration is open for the 19th IOA World<br />
Congress in Tokyo August 31-September 3,<br />
20<strong>09</strong><br />
To register on line visit<br />
https://apollon.nta.co.jp/ozone-20<strong>09</strong>-er/<br />
To make hotel reservations visit<br />
https://apollon.nta.co.jp/ozone-20<strong>09</strong>-eh/<br />
Note: Some hotel room dates are limited,<br />
so you should make your reservations<br />
quickly.<br />
OZONE . . .<br />
<strong>Ozone</strong> Water Systems is pleased to<br />
announce UL 508A Shop Status!<br />
480.421.2400 Tel. 480.421.2300 Fax.<br />
www.ozonewatersystems.com<br />
5401 S. 39th Street, Suite 1, Phoenix, AZ 85040<br />
. . . DONE RIGHT<br />
SALES � SERVICE � MONITOR CALIBRATION � CONTACT EQUIPMENT<br />
SERVICE CONTRACTS � EMERGENCY SERVICE � SPARE PARTS � RENTALS<br />
Page 4<br />
INDEX OF ADVERTISERS<br />
2 AirTree <strong>Ozone</strong> Technology<br />
7 Analytical Technology Inc.<br />
8,9 BMT Messtechnik GmbH<br />
20 Bollyky Associates Inc.<br />
5 Eco Sensors, Inc.<br />
24 IN USA Inc.<br />
6 Mazzei Injector Corporation<br />
4 <strong>Ozone</strong> Water Systems<br />
40 Ozonia/ Degremont Technologies<br />
10 Plasma Technics, Inc.<br />
14 SeQual Technologies<br />
39 Teledyne API<br />
11 Tessenderlo Kerley<br />
Copyright© 20<strong>09</strong> <strong>International</strong> <strong>Ozone</strong> Association. All rights reserved. No<br />
part of this publication may be reproduced, stored, transmitted, or<br />
disseminated in any form or by any means without prior written permission<br />
from the <strong>International</strong> <strong>Ozone</strong> Association. The publisher assumes no<br />
responsibility for any statements of fact or opinion expressed in the published<br />
papers.
<strong>Ozone</strong> News Volume 37, No 3<br />
Editor’s Notes<br />
IOA members have a special opportunity this<br />
summer – attending the 19th World Congress and<br />
Exposition, Tokyo, Japan, August 31-September 9,<br />
20<strong>09</strong>. IOA World Congresses are held every two<br />
years, but in Japan only about every twelve years.<br />
The Nippon Islands Group of IOA and the Japan<br />
<strong>Ozone</strong> Association have been working hard to<br />
make this a memorable Congress. The technical<br />
program will consist of three parallel sessions with<br />
159 oral technical presentations and several poster<br />
presentations, from 17 countries. There will be four<br />
separate sessions with 22 presentations on medical<br />
applications.<br />
Attendees will have the option of devoting one<br />
afternoon to technical tours of one water treatment<br />
plant and one wastewater treatment plant that<br />
utilize ozone. A special technical tour is planned<br />
after the conference to visit water and wastewater<br />
treatment plants in the Kyoto area as well tour this<br />
remarkable city.<br />
For accompanying persons, there will be<br />
opportunity for sightseeing tours on each day of the<br />
conference. The organizers have selected the very<br />
nice Hotel Grand Palace, located close to Tokyo<br />
Imperial Palace and Gardens. There is convenient<br />
shuttle bus transportation from Tokyo’s Narita<br />
airport to the hotel.<br />
The conference is being held at Tower Hall<br />
Funabori. Funabori is very easily reached by<br />
subway, without any transfers, with a station<br />
located just outside the hotel; Tower Hall is also just<br />
next to the subway station. Japan IOA will have<br />
representatives at the hotel to help delegates<br />
negotiate the subway system. (We tried it last year,<br />
and it was very easy)<br />
A gala night is planned at the conclusion of the<br />
conference. This is sure to be a memorable<br />
occasion.<br />
Detailed information and a preliminary program for<br />
the Congress are enclosed in this issue of <strong>Ozone</strong><br />
News. The most convenient way to register for the<br />
Page 5<br />
conference is online by assessing any IOA website<br />
(www.io3a.org, www.ioa-ea3g.org) I hope you can<br />
attend. You will find it a remarkable experience.<br />
Barry Loeb<br />
Opening reception - Boston Conference
<strong>Ozone</strong> News Volume 37, No 3<br />
Emerging Contaminant Survey<br />
The EPA is seeking approval from the Office of<br />
Management and Budget to collect samples and conduct<br />
a survey of approximately 25 utilities to help determine<br />
to prevalence of about 200 emerging contaminants in<br />
drinking water. Improved chemical analyses will be used<br />
to detect many pharmaceuticals including antidepressants<br />
and for such substances as flame retardants showing up in<br />
wastewater. The water samples will also be tested for<br />
fluorinated compounds such as perfluorooctanoic acid<br />
(PFOA). PFOA is used in the manufacture of Teflon and<br />
has shown up in drinking water. For more information,<br />
refer to Federal Register, April 8, 20<strong>09</strong>, pp 15965-15967.<br />
Industry News<br />
Page 6<br />
Reference Document – Best Available<br />
Technologies<br />
The European community is undertaking a process for<br />
the revision of the Reference Document on Best<br />
Available Techniques (BATs) in Common Waste Water<br />
and Waste Gas Treatment/Management Systems in the<br />
Chemical Sector (CWW BREF) associated to the<br />
European Directive Integrated Pollution Prevention and<br />
Control (IPPC). Dr. Sylvie Baig, IOA Treasurer and<br />
President-Elect is part of the working group to inform<br />
them on applicable ozone technologies with the aim to<br />
have them recommended within the BATs.<br />
BAT embrace the most effective and suitable measures<br />
for achieving a high general level of protection of the<br />
environment as a whole against emissions. Non-
<strong>Ozone</strong> News Volume 37, No. 3<br />
• Drying at the point of sample by<br />
Peltier-electric cooling<br />
• Eliminates the potential for<br />
condensation in the sample line<br />
• Based on our successful BMT 964<br />
• Low flow warning<br />
Industry News (cont’d)<br />
biodegradable abatement techniques to be considered as<br />
part of BAT include oxidation, reduction, hydrolysis, air<br />
oxidation and incineration. <strong>Ozone</strong> will be considered as<br />
part of BAT oxidation techniques.<br />
Mazzei Pipeline Flash Reactor<br />
Mazzei Injector Company announces the addition of its<br />
Pipeline Flash Reactor (PFR) for post-treatment<br />
aeration of pure-oxygen injection in wastewater treatment<br />
applications. The compact system utilizes a small<br />
sidestream passed through a patented Mazzei Injector to<br />
draw in ambient air or concentrated oxygen. The Aerated<br />
sidestream is delivered to the reactor where it<br />
aggressively mixes with the main flow, uniformly<br />
transferring the oxygen in the effluent pipeline. The PFR<br />
eliminates the need for post-treatment cascading systems<br />
or diffuser basins. It can also be utilized to dissolution of<br />
• Fully automatic condensate removal<br />
• <strong>Ozone</strong> resistant sample gas pump<br />
• <strong>Ozone</strong> catalyst not needed<br />
• Measurement ranges available<br />
down to 5 g/Nm (2500 ppm )<br />
3<br />
v<br />
OZONE IN OFF-GAS<br />
BACK<br />
SCROLL / SET<br />
ZERO / ENTER<br />
OZONE ANALYZER BMT 964<br />
WARM LOW FLOW<br />
Measuring the ozone content in an ozone process off-gas requires proper sample gas conditioning. Typically,<br />
operating parameters and ambient conditions differ from site to site. If you are concerned about reliable and<br />
accurate measurement of ozone in off-gas, please call and ask for the BMT OZONE-IN-OFF-GAS SYSTEM<br />
BMT MESSTECHNIK, BERLIN<br />
OSTI, MONTEREY<br />
Off-Gas <strong>Ozone</strong> Content<br />
is a Valuable Process Parameter!<br />
Page 8<br />
oxygen gas in systems with high, dissolved oxygen<br />
requirements. For more information, visit<br />
www.mazzei.net.<br />
Pipeline flash reactor<br />
DH5<br />
COOL<br />
WARM<br />
MAX.<br />
POWER<br />
BMT<br />
OZONE-IN-OFF-GAS<br />
ANALYSIS<br />
BMT MESSTECHNIK GMBH - Güterfelder Damm 87-91 - D-14532 Stahnsdorf, Germany - Phone +49-3329-69677-0 - www.bmt-berlin.de<br />
OSTI Inc. (<strong>Ozone</strong> Systems & Technology Int'l) - P.O. Box 3320 - Monterey, CA 93942 - Phone +1-831-649 1141 - www.osti-inc.com<br />
UP<br />
SAMPLE-GAS<br />
DEHUMIDIFIER<br />
DH5<br />
BMT MESSTECHNIK, BERLIN<br />
OSTI, MONTEREY, CA
<strong>Ozone</strong> News Volume 37, No. 3<br />
BACK<br />
SCROLL / SET<br />
ZERO / ENTER<br />
OZONE ANAL Y ZER BMT 964<br />
OZONE ANAL Y ZER BMT 964<br />
BMT MESSTECHNIK, BERLIN<br />
OSTI, MONTEREY<br />
BMT MESSTECHNIK, BERLIN phone +49 - 30 - 801 85 95 fax +49 - 30 - 802 23 62<br />
8 Out Common<br />
9 Lamp Low<br />
12 High Alarm<br />
13 Low Alarm<br />
14 Cuvette Dirty<br />
2 Purge<br />
Isolated, U =28 V, I =0.5 A<br />
max max<br />
RELAY CONTACTS:<br />
OUTPUTS:<br />
10 Zero GND<br />
Isolated, U =24 VDC, I = 18 mA<br />
INPUT:<br />
USE SHIELDED CABLE CONNECT SHIELD TO<br />
ALWAYS CONSULT THE MANUAL<br />
OUTPUT AND CONTROL TERMINALS<br />
ANALOG OUTPUTS:<br />
Open on Error<br />
Isolated, U =30 VDC, I =1A<br />
max max<br />
7 Concentration 0-10V<br />
6 GND (10 V)<br />
5 Concentration 4-20 mA<br />
4 GND (4-20 mA)<br />
ERROR RELAY:<br />
Isolated<br />
1<br />
3<br />
BACK<br />
SCROLL / SET<br />
RELAY CONTACTS:<br />
OUTPUTS:<br />
OUTPUT AND CONTROL TERMINALS<br />
OZONE ANAL Y ZER BMT 964<br />
BMT MESSTECHNIK, BERLIN phone +49 - 30 - 801 85 95 fax +49 - 30 - 802 23 62<br />
8 Out Common<br />
9 Lamp Low<br />
12 High Alarm<br />
13 Low Alarm<br />
14 Cuvette Dirty<br />
2 Purge<br />
Isolated, U =28 V, I =0.5 A<br />
max max<br />
10 Zero GND<br />
Isolated, U =24 VDC, I = 18 mA<br />
INPUT:<br />
USE SHIELDED CABLE CONNECT SHIELD TO<br />
ALWAYS CONSULT THE MANUAL<br />
BMT MESSTECHNIK, BERLIN<br />
OSTI, MONTEREY<br />
ZERO / ENTER<br />
OZONE ANALYZER BMT 964<br />
Page 9<br />
Isolated, U =30 VDC, I =1A<br />
max max<br />
7 Concentration 0-10V<br />
6 GND (10 V)<br />
5 Concentration 4-20 mA<br />
4 GND (4-20 mA)<br />
ANALOG OUTPUTS:<br />
If you are Tired of<br />
Battling Service Related Issues<br />
• Three year warranty, on all parts & labor,<br />
including the UV lamp<br />
• Containing over twenty years of experience in<br />
designing highest quality UV photometers<br />
• Our masterpiece: OZONE ANALYZER BMT 964<br />
Panel mount, portable, and wall mount models<br />
•<br />
Industry News (cont’d)<br />
Trojan Technologies forms VIQUA<br />
Trojan Technologies has announced that they have<br />
changed their residential water treatment business unit<br />
name to VIQUA – a Trojan Technologies Company<br />
effective immediately.<br />
“This will allow us to better position the company's<br />
market-facing business,” says Ron Braun, managing<br />
director. “As the residential center for water treatment<br />
excellence, we provide a broad spectrum of solutions to<br />
our customers who are facing water quality issues. This<br />
new brand will allow us more flexibility as we grow and<br />
expand that market.”<br />
Key product lines Sterilight® and TrojanUVMAX<br />
will lead the business toward a strict focus on residential<br />
water treatment solutions, advanced research and<br />
development and only the highest quality customer<br />
support. Trojan Technologies acquired R-Can<br />
•<br />
•<br />
Open on Error<br />
ERROR RELAY:<br />
State-of-the-art design, best materials<br />
Unprecedented accuracy, stability, and reliability<br />
through design competence<br />
• Proven by thousands of installations around the world<br />
• The companion to your PC or PLC<br />
Environmental Inc in August 2008. The residential<br />
business will continue to operate out of Guelph, Ontario<br />
with approximately 90 employees.<br />
Isolated<br />
ENMET Introduces Carbon Dioxide Sensor<br />
The EX-5165 Sensor/Transmitter features an infrared<br />
sensor which can be supplied calibrated for the detection<br />
of carbon dioxide in ranges available from 0-500 ppm to<br />
0-100% by volume CO 2. The NDIR sensor can<br />
continuously monitor high concentrations of CO 2 and<br />
operate in an anaerobic environment. This<br />
sensor/transmitter provides an LCD of the gas<br />
concentration and has three LED alarm point indicators.<br />
It is approved for location in Class I, Division 1, Groups<br />
B, C and D atmospheres. For more information, contact<br />
ENMET Corporation at info@enmet.com or<br />
www.enmet.com.<br />
1<br />
3<br />
RANGE<br />
SER. NO.<br />
BMT MESSTECHNIK, BERLIN<br />
OZONE CONTENT<br />
BACK<br />
SCROLL / SET<br />
BMT MESSTECHNIK, BERLIN<br />
OSTI, MONTEREY<br />
ZERO / ENTER<br />
OZONE ANALYZER BMT 964<br />
• Built-in sample gas filter<br />
• Calibration error less than 0.5% of range<br />
3<br />
• Ranges from 0-2to0-400g/Nm<br />
3<br />
• Selectable dimensions: g/Nm , %wt/wt, ppmv<br />
• Programmable via front panel and RS-232<br />
• Full internal diagnostics<br />
• Event and Error Log with date and time stamp<br />
• Windows software for easy control included<br />
• Power supply: 85 - 264 VAC or 12 - 36 VDC<br />
BMT MESSTECHNIK GMBH - Güterfelder Damm 87-91 - D-14532 Stahnsdorf, Germany - Phone +49-3329-69677-0 - www.bmt-berlin.de<br />
OSTI Inc. (<strong>Ozone</strong> Systems & Technology Int'l) - P.O. Box 3320 - Monterey, CA 93942 - Phone +1-831-649 1141 - www.osti-inc.com
<strong>Ozone</strong> News Volume 37, No.3<br />
Report from Boston Conference<br />
On May 3-6, 20<strong>09</strong> some 322 delegates from 10 countries<br />
attended the joint <strong>International</strong> <strong>Ozone</strong> Association and<br />
<strong>International</strong> Ultraviolet Association Conference at the<br />
Hyatt Regency, Cambridge Massachusetts. This was the<br />
second joint conference between the IOA and IUVA, with<br />
the first being the Los Angeles World Congress in 2007.<br />
Page 10<br />
The hotel was an excellent venue, located on the Charles<br />
River. University rowers were practicing in the river each<br />
morning. For those exploring the city, the hotel was in a<br />
very central location.<br />
Paul Overbeck, Executive Director IOA and IUVA<br />
opened the conference and welcomed delegates and<br />
outlined the program. He thanked CDM for their<br />
sponsorship of the opening reception the evening before.<br />
Linda Gowman, IUVA president commented that IUVA is<br />
now 10 years old and has 525 members worldwide. She<br />
stressed the need for broader membership. There is a<br />
need to reduce carbon footprints. We do not yet know<br />
what delivering sustainable water means.<br />
Jeff Neemann, IOA President welcomed those attending<br />
an IOA conference for the first time. He thanked Paul<br />
Overbeck and Diana Schoenberg for their efforts in<br />
coordinating the conference. He stressed the need for<br />
volunteerism in our technical societies. He then had a<br />
hilarious cell phone “conversation” with President
<strong>Ozone</strong> News Volume 37, No. 3<br />
Obama regarding the universal nature of ozone<br />
applications.<br />
Achim Reid, WEDECO, the Primary Sponsor of the<br />
conference also welcomed attendees and encouraged<br />
interaction between all to share experiences and<br />
expertise.<br />
Dan LaPrade of the Massachusetts Department of<br />
Environmental Protection summarized in a keynote<br />
address the use of ozone and UV in Massachusetts<br />
drinking water plants. Currently, 87% of MA water<br />
treatment plants use chlorine only, 16% use ozone. There<br />
currently is substantial interest in UV for disinfection.<br />
Wastewater plants may start using ozone or UV as they<br />
cannot switch to a dechlorination agent. There is a need<br />
for ozone and UV to be adapted to small systems.<br />
Frederick Laskey, Executive Director, Massachusetts<br />
Water Research Authority (MWRA) in a second keynote<br />
address summarized the history of the Boston Water<br />
Supply. MWRA is currently responsible for 220MGD<br />
drinking water (peak 350MGD) and 350 MGD<br />
wastewater (Peak 1200MGD). The authority currently<br />
Page 11<br />
has excess water due to reduced demand as a result of<br />
conservation and pricing.<br />
Boston was known as the dirtiest harbor in the USA. In<br />
2002 the $3.8 billion Boston Harbor Project, which<br />
reduced contamination of the harbor was completed. It is<br />
projected that Boston will have the cleanest urban<br />
beaches in the USA by 2011.<br />
The Carroll Water Treatment plant, utilizing ozone, was<br />
completed in 2005. The Authority saw immediate taste<br />
and odor improvements. In fact, in a nationally televised<br />
taste test between the Carroll water and bottled water, the<br />
Carroll water was preferred. Boston water is currently<br />
pharmaceutical free.<br />
The Authority is now working to comply with the LT2<br />
requirements for surface water. It is anticipated that UV<br />
will be used for a second stage disinfection. The project<br />
is expected to bid in 2011 and be completed in 2014.<br />
Technical Program<br />
Three parallel sessions were held with a total of 80<br />
Why not modernize your treatment process and go green with Captor?<br />
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<strong>Ozone</strong> News Volume 37, No.3<br />
technical papers presented. There were also 10 poster<br />
presentations.<br />
Technical topics covered were:<br />
• Advanced Oxidation of Contaminants<br />
• AOP and <strong>Ozone</strong> Byproducts<br />
• Modeling UV Systems<br />
• <strong>Ozone</strong> Case Studies<br />
• <strong>Ozone</strong> Design and Operation<br />
• <strong>Ozone</strong> Design and Operation<br />
• Perozone and AOP Processes<br />
• UV Case Studies<br />
• UV Disinfection Design<br />
• UV Disinfection Research<br />
• UV Regulatory<br />
• UV Validation<br />
Exhibition<br />
The conference had a very extensive exhibition with 27<br />
exhibitors from at least 6 countries. It was gratifying to<br />
see many first-time exhibitors and well as the long-term<br />
exhibitors.<br />
A highlight of the exposition event was the Spring Fling<br />
Reception held on Monday night in the exhibition hall.<br />
Companies exhibiting were:<br />
AirSep Corporation<br />
Aquafine Corporation<br />
Aquionics, Inc.<br />
Astro Pak Corporation<br />
Calgon Carbon Corporation<br />
Electrolytic <strong>Ozone</strong>, Inc.<br />
Fuji – Water Treatment Division<br />
Page 12<br />
Guardian Manufacturing<br />
IN USA Corp.<br />
ITT Water & Wastewater<br />
Kerfoot Technologies, Inc.<br />
Light Sources, Inc.<br />
Mazzei Injector Company<br />
Mitsubishi Power Products, Inc.<br />
Nedap Light Controls<br />
OSTI, Inc.<br />
Oxygen Generating Systems, Int’l<br />
<strong>Ozone</strong> Solutions, Inc.<br />
<strong>Ozone</strong> Water Systems<br />
Ozonia North America<br />
Pacific Consolidated Industries<br />
Plasma Technics, Inc.<br />
Severn Trent Services<br />
Statiflo Corporation<br />
Teledyne – API<br />
The <strong>Ozone</strong> Man, Inc.<br />
Trojan Technologies<br />
Facility Tours<br />
There were two technical tour options for this conference.<br />
The ozone technical tour included the Walter J. Sullivan<br />
Water Purification Facility at the Cambridge Water<br />
Department and the MWRA John Carroll Water<br />
Treatment Plant. There was also an <strong>Ozone</strong> Operations<br />
Workshop at the Carroll WTP.<br />
The UV technical tour included the Brockton, MA<br />
Advanced Waste Water Treatment Plant and the<br />
Pawtucket, RI Water Treatment Plant.
<strong>Ozone</strong> News Volume 37, No.3<br />
The Sullivan facility is designed for 24MGD with<br />
capability to expand to 30MGD and was commissioned<br />
in 2001. The plant serves 100,000 people and has<br />
reservoirs for 8 months supply. The plant uses dissolved<br />
air floatation (in cold weather) intermediate ozonation<br />
and biological filtration. <strong>Ozone</strong> is supplied by (3) 400<br />
ppd oxygen fed generators (WEDECO), operated<br />
seasonally. Bromides are not an issue in this plant.<br />
The Carroll facility has a capacity of 465 MGD with<br />
average production of 270MGD. The plant produces<br />
unfiltered water into 7 new colored storage facilities.<br />
<strong>Ozone</strong> is used for primary disinfection. The plant was<br />
designed for 3 log giardia inactivation and 2 log<br />
cryptosporidium inactivation. Eventually UV will be<br />
needed for final disinfection. The plant has (4) 3380<br />
lb/day Fuji <strong>Ozone</strong> Generators producing 10% ozone from<br />
oxygen. In winter, half of the plant is shut down for<br />
maintenance. When UV is installed, the ozone dosage for<br />
giardia inactivation will be reduced.<br />
This plant, its design and layout was very impressive. The<br />
ozone generators are some of the largest manufactured.<br />
Sponsors<br />
The 20<strong>09</strong> Boston Conference Technical Program<br />
Committee extends their thanks and appreciation to the<br />
following sponsors who made this educational event<br />
possible.<br />
Platinum<br />
ITT Water & Wastewater www.usittwww.com<br />
Gold<br />
CDM www.cdm.com<br />
Ozonia North America www.ozonia.com<br />
Silver<br />
AECOM www.aecom.com<br />
Black & Veatch www.bv.com<br />
Calgon Carbon Corp. www.calgoncarbon-us.com<br />
Fuji Electric www.fujielectric.com<br />
Hazen & Sawyer www.hazenandsawyer.com<br />
Jordon, Jones & Goulding www.jjg.com<br />
MWRA www.mwra.state.ma.us<br />
Severn Trent Services www.severntrentservices.com<br />
Trojan Technologies www.trojanuv.com<br />
Page 13<br />
Bronze<br />
AirSep Corp. www.airsep.com<br />
CH2m Hill www.ch2m.com<br />
Kennedy/Jenks www.kennedyjenks.com<br />
Mitsubishi Electric Power Products, Inc.<br />
www.meppi.com<br />
Oxygen Generating Systems, Intl. www.ogsi.com<br />
Transdyn www.transdyn.com<br />
Technical Program Committee<br />
The Technical Program Committee was responsible for<br />
solicitation, selection and organization of the 80 papers<br />
and 10 poster presentations. This is the heart of the<br />
conference and their efforts are appreciated.<br />
• Mohamed Gamal El-Din, Ph. D., P. Eng., University<br />
of Alberta, Co-chair (IOA)<br />
• Karl Linden, Ph. D., University of Colorado at<br />
Boulder, Co-chair (IUVA)<br />
• Jim Bolton, Ph. D., Bolton Photosciences<br />
• Pamela Chelme-Ayala, Ph. D., University of Alberta<br />
• Theping Chen, AECOM<br />
• Jim Constantacos, Constant America<br />
• Larry Forney, Ph. D., Georgia, Tech.<br />
• Ronald Gehr, Ph. D., McGill University<br />
• Dennis Greene, Ph. D., AECOM Water<br />
• Mirat Gurol, Ph. D., San Diego State University<br />
• Ron Hoffman, Ph. D., University of Toronto<br />
• Paul Overbeck, IOA & IUVA<br />
• Erik Rosenfeldt, Ph. D., University of Massachusetts<br />
– Amherst<br />
• Mike Santelli, Light Sources, Inc.<br />
• Diana Schoenberg, IOA & IUVA<br />
Proceedings<br />
Proceeding from this conference are available from the<br />
Pan American Group for $75 member and $125 non<br />
member. For more information, contact PAG at<br />
info@ea3g.org.
<strong>Ozone</strong> News Volume 37, No.3<br />
Full Scale Application of a Novel Sludge Ozonation Process for<br />
Achieving 40% and up to 80% Excess Sludge Reduction at a<br />
25,000 m 3/day Municipal Wastewater Plant<br />
Gunther Raugust 1, Luciano Liberati 2, Richard Novak 3, Peter Wrampe 4<br />
1 Praxair Deutschland GmbH & Co. KG, Schnellerstrasse 6-13, 12439 Berlin, Germany<br />
2 Rivoira SpA, Via Durini 7, 20122 Milano, Italy<br />
3 Praxair, Inc. 7000 High Grove Boulevard. Burr Ridge, IL 60527, US<br />
498 Pipers Hill Road, Wilton, CT 06897, US<br />
(Correspondence should be addressed to e-mail: gunther_raugust@praxair.com)<br />
Introduction<br />
The activated sludge process is the most widely utilized<br />
method for wastewater treatment process due to its<br />
relatively low cost and relative ease of operation. The<br />
generation of excess sludge is an inevitable result of the<br />
biochemical processing of organic waste by microbial<br />
agents in the activated sludge process. Generally the<br />
excess sludge produced from the conventional aerobic<br />
biological wastewater treatment process ranges from 0.2-<br />
0.4 kg excess solids/kg COD removed depending on the<br />
Solids Retention Time (SRT), oxic state and microbial<br />
species distribution in the treatment system. The<br />
associated power and chemicals costs for solids handling<br />
and eventual disposal can be significant and as much as<br />
40-60% of the costs of wastewater treatment are<br />
associated with the handling and disposal of excess solids<br />
(Tchobanoglous et al, 2003).<br />
Several factors have emerged which increase the<br />
likelihood that sludge costs will continue to increase. For<br />
instance restrictions on the availability of landfills (In<br />
Germany f.e. TASi 2001 (Verwaltungsvorschrift<br />
Technische Anleitung zur Verwendung, Behandlung und<br />
sonstigen Entsorgung von Siedlungsabfällen)),<br />
restrictions on the quality of biosolids used in land<br />
application and increasing citizen concerns over odor are<br />
causing sludge handling costs to increase. Recent<br />
regulatory pressures seem likely to increase the costs<br />
associated with sludge disposal. In the EU for instance,<br />
Abstract<br />
Although sludge ozonation in lab scale tests have tended to yield economic dosage rates in the regime of ≤ 0.1 kg O 3/kg SS<br />
removed, previous attempts to extend the approach to commercial scale installations have resulted in non-economical ozone<br />
dosage levels (Sievers et al, 2004; Yasui et al, 1996; Kobayashi et al, 2001; Sakai et al, 1997), requiring as much as 0.395 kg<br />
O 3 per kg SS removed (See Table 2). In this paper, we discuss a novel approach to sludge ozonation and report the results of<br />
full scale tests carried out at a 7 MGD (1100 m³/h) wastewater treatment facility which has been in operation since May 2006.<br />
A cost effective <strong>Ozone</strong> consumption value of 0.07 kg O 3/kg SS reduced was attained in the field, demonstrating the successful<br />
translation of bench scale type results to field applications using the Praxair approach.<br />
Page 15<br />
while regulatory pronouncements like the Urban Waste<br />
Water Treatment Directive 91/271/EEC which requires<br />
that most of the EU populations be served by wastewater<br />
treatment facilities are leading to the generation of more<br />
excess sludge, other regulations like the Sewage Sludge<br />
Directive 86/278/EWG places restrictions on the<br />
agricultural application of sludge from the wastewater<br />
treatment process, while the landfill directive<br />
1999/31/EC effectively limits the disposal routes for<br />
excess sludge (Perez-Elvira et al, 2006).<br />
While the wastewater industry has traditionally focused<br />
on technologies that reduce the excess sludge generated<br />
at the back end of the wastewater treatment process, there<br />
has lately been a renewed interest in technologies focused<br />
on fundamentally reducing the generation of sludge in the<br />
aeration basin (WERF, 2004; Perez-Elvira et al, 2006).<br />
Overview - Sludge Ozonation<br />
Although several methods exist for achieving sludge<br />
minimization, the sludge ozonation process has been<br />
extensively studied and characterized, and has shown<br />
immense promise as a viable method for attaining<br />
consistent and reliable reduction of excess sludge (Yasui<br />
et al, 1996). The basic concept is the application of ozone<br />
to a side stream containing at a minimum, the equivalent<br />
portion of the excess sludge to be eliminated. The<br />
application of ozone to this stream causes the bacterial<br />
cells that come in contact with ozone to be lysed (Figure
<strong>Ozone</strong> News Volume 37, No.3<br />
1). Upon lysis, the cellular COD that is contained within<br />
the cells is leaked out, and the lysis products are then<br />
recycled back to the aeration basin where the bacteria<br />
feed on the released COD. The effective reduction in<br />
excess sludge is achieved when the COD generated from<br />
the lysed VSS (bacterial cells) is bio-oxidized in the<br />
aeration basin. The lysis COD when consumed,<br />
effectively generate a quantity of excess cells determined<br />
by the yield obtained within the wastewater treatment<br />
system.<br />
Figure 1. Principle of ozone lysis versus mineralization<br />
While the conceptual case for sludge ozonation and other<br />
lysis based approaches is straightforward, and a<br />
significant amount of work has been done both at the lab<br />
and field scales, the sludge ozonation process has been<br />
slow to be adopted, largely because the amounts of ozone<br />
required to effect the sludge reduction are uneconomical.<br />
<strong>Ozone</strong> consumption values required to achieve cell lysis<br />
have ranged from about 0.165-0.395 Kg O 3/Kg TS<br />
removed (Yasui et al, 1996; Ried et al, 2002). Although<br />
the economical range of ozone consumption will<br />
necessarily depend on localized costs for sludge handling<br />
and disposal, we estimate that the range of ozone<br />
consumption that will be viable will be in the regime of<br />
≤ 0.1 kg O 3/kg TS removed. The cost for sludge handling<br />
and disposal can vary between < € 80/dry t TS as a low<br />
cost range and > € 400dry t TS as a high cost range. The<br />
operational cost for generating 1 kg ozone using oxygen<br />
can be estimated as € 1 to 1.6. With an ozone<br />
consumption demand of 0.1 kg O 3/ kg TS removed, a<br />
total ozone demand of 100 kg ozone/ dry t TS is needed.<br />
This leads to operational costs of 100 to 160 €/dry ton TS.<br />
Previous studies have indicated the possibility that sludge<br />
Page 16<br />
ozonation can have a deleterious impact on several key<br />
operational parameters of the wastewater treatment<br />
process. Ried et al (2002) observed an increase in the<br />
effluent COD levels following sludge ozonation. Böhler<br />
& Siegrist (2004) have reported on the inhibition of<br />
nitrification and the improvement of denitrification<br />
observed during the sludge ozonation process. Raugust &<br />
Schwerdt (2004) reported about the possibility to<br />
completely eliminate filamental bacteria in the system.<br />
Bench Scale Tests<br />
Materials and Methods<br />
Prior to commencing pilot tests in the field, initial bench<br />
scales tests were carried out in a 1.5” diameter sludge<br />
ozone contact unit. The bench scale tests were undertaken<br />
in order to establish the effects of different contacting<br />
configurations on the ozone dosage requirements, lysis<br />
effect of ozone contacting, COD release associated with<br />
the lysis process as well as the correlation of the COD<br />
release with the extent of VSS degradation achieved and<br />
the biodegradability of the COD released as a result of the<br />
lysis process.<br />
Biodegradability was determined by comparing the<br />
oxygen uptake rates for the lysis products vs. a synthetic<br />
wastewater sample. Oxygen Uptake Rate (OUR) tests<br />
were carried out in a computerized N-CON Respirometer.<br />
Wastewater sludge samples were obtained from a<br />
municipal wastewater plant (Illinois, USA) with influent<br />
made up predominantly of sanitary wastewater. A 1L<br />
sample of synthetic wastewater was made up in distilled<br />
water by adding 16 g peptone, 11 g meat extract, 3 g<br />
Urea, 0.7 g NaCl, 0.4 g CaCl 2.2H 2O, 0.2 g MgSO 4.7H 2O,<br />
2.8 g K 2HPO 4. The resulting wastewater was then diluted<br />
as required.<br />
Full Scale Tests<br />
The Lariana WWTP (25,400 m 3/day; 10,000 kg/day COD<br />
removed – 2006 average) is located in Bulgarograsso<br />
(Como, Italy) and treats wastewater characterized by a<br />
predominant industrial (mainly textile) component: 62%<br />
as hydraulic flow rate and 75% as COD load during dry<br />
weather. The plant is a two-train aeration basin operation,<br />
with processes that includes an activated-sludge process<br />
for biological nitrogen removal (single sludge anoxic predenitrification<br />
- aerobic nitrification), followed by a sand<br />
filtration process for suspended solid removal, and final
<strong>Ozone</strong> News Volume 37, No.3<br />
effluent ozonation for the removal of color and<br />
surfactants. Prior to the commencement of the sludge<br />
ozonation process, all of the return activated sludge<br />
(RAS) was recycled to the anoxic pre-denitrification<br />
basin. The excess sludge is held in an aerobic holding<br />
tank and is then subsequently thickened and dewatered to<br />
about 19% dry solids content. The historical (2 year<br />
average) yield at the plant was 0.35 kg TS/kg COD<br />
removed.<br />
Figure 2. Generic schematic of the Praxair Sludge<br />
Ozonation Process<br />
Praxair’s sludge ozonation process Lyso TM comprises of<br />
an ozone supply system, a pump, and a gas liquid<br />
contacting system within which the sludge-ozone contact<br />
occurs (see Figure 2). The process requires that a portion<br />
of the RAS is passed through the sludge ozone contactor.<br />
System conditions are carefully controlled to ensure that<br />
an amount of ozone sufficient to implement the lysis of<br />
the bacterial cells is applied. An Allen Bradley SLC5/03<br />
PLC system was used to provide automatic control of the<br />
process. <strong>Ozone</strong> was generated from pure oxygen. A 3-4<br />
kg/h flow of a 7-8% w/w O 3 gas stream was applied to the<br />
portion of the RAS stream that flowed through the<br />
contactor. Because the primary RAS line at the<br />
Bulgarograsso plant is returned to an anoxic<br />
denitrification basin rather than to the nitrification basins,<br />
a separate RAS flow needed to be established for the<br />
sludge ozonation process as the high oxic state of the<br />
ozonated sludge implies that this stream cannot be<br />
directly returned to an anoxic basin. Ozonated sludge was<br />
returned to both nitrification basins. Detailed<br />
microbiological and respirometric analyses were<br />
undertaken throughout the tests.<br />
Page 17<br />
Bench Scale Tests<br />
Results<br />
Figure 3. Baseline tests comparing OUR signature of<br />
sludge exposed to (synthetic) wastewater sample<br />
containing an ideal nutrient mix vs. a blank sample<br />
containing tap water.<br />
Figure 4. Extended 30-hour OUR profile of municipal<br />
wastewater and lysis COD products<br />
An OUR baseline was determined by comparing the<br />
OUR of a synthetic wastewater containing an ideal<br />
nutrient mix with tap (blank) water (Figure 3). The<br />
endogenous respirometric rate for the sludge sample was<br />
determined from the OUR measurements obtained using<br />
the blank. Following the sludge ozonation process, lysis<br />
products were collected and the nutrient composition was<br />
analyzed (see Table 1). By comparing the relative<br />
proportions of Nitrogen and Phosphorus to the COD<br />
present in the lysis COD, it was determined that the<br />
nutrient composition of the lysis products was very<br />
similar to that of the idealized synthetic wastewater.
<strong>Ozone</strong> News Volume 37, No.3<br />
Table 1. Relative proportions of the composition of phosphorus and nitrogen compared to the COD present in wastewater<br />
influent, lysis products and synthetic wastewater formulations. Lysis products are derived from samples.<br />
Figure 4 above summarizes the results of the<br />
biodegradability tests that were run on the lysis products.<br />
The OUR results confirm the high biodegradability of the<br />
lysis product.<br />
Full Scale Tests<br />
Prior to the commencement of the sludge ozonation<br />
process, a comprehensive baselining study was<br />
undertaken during which the process conditions at the<br />
plant were measured and compared to the historical plant<br />
data. Broad agreement was observed between the results<br />
of the baselining exercise and the historical plant data. A<br />
plant wide biosolids inventory had also been established<br />
prior to the commencement of the tests, and a critical<br />
control feature was to maintain this solids inventory at<br />
constant levels in order to facilitate accurate accounting<br />
for the fate of the solids in the process. Solids inventory<br />
was therefore maintained at 80,000 kg and the extent of<br />
sludge reduction achieved was obtained by closing the<br />
solids balance. It was already established from the<br />
analysis of the previous 2 year operating data at the plant<br />
that the average yield was 0.35kg TS/kg COD removed.<br />
The current levels of sludge generation were compared<br />
against this historical baseline to determine the extent of<br />
sludge reduction achieved.<br />
Discussion<br />
The pilot test was carried out at a scale that was designed<br />
to allow for the effective treatment of up to 40% of the<br />
excess sludge. Praxair’s approach to sludge ozonation<br />
differs from previous methods in its high selectivity<br />
(Fabiyi & Novak, 2007) derived largely from the use of a<br />
plug flow approach that maximizes the use of ozone for<br />
cell lysis rather than wasteful consumption of ozone by<br />
the chemical oxidation of the lysis products. Our<br />
approach uses multiple injection loops for bringing the<br />
sludge and the ozone rich gas stream in contact. The<br />
Page 18<br />
ozone consumption observed during the tests was<br />
approximately 0.07 kg of O 3 per kg TSS reduced. Table 2<br />
provides a comparative summary of the ozone<br />
consumption values obtained during this study and other<br />
results from the literature.<br />
Table 2. Comparative table of specific ozone<br />
consumption and the corresponding sludge reduction<br />
(derived from Sievers et al, 2004).<br />
We observed significant reduction of foaming in the<br />
aeration basin process of the wastewater treatment<br />
operation as a result of the ozonation process. Prior to the<br />
commencement of the ozonation process, there was a<br />
persistent 20 cm foam layer at the top of the aeration<br />
basin causing solids to be frequently purged from the<br />
surface of the aeration tank and sent directly to an aerobic<br />
sludge holding tank that is connected to the aeration basin<br />
through an overflow weir. Following the commencement<br />
of the ozonation process, there was a significant<br />
reduction in the population of all filamentous microbial<br />
species, with the most significant reductions being<br />
observed in Microthrix parvicella and Nocardia species<br />
(see Figure 5). The impact of the sludge ozonation<br />
process on filamentous organisms was rapid and there<br />
was an effective control of the foaming within the first<br />
three weeks of operations.<br />
Although previous studies (e.g., Ried et al, 2002) had<br />
indicated that there was a slight increase in the effluent<br />
COD during sludge ozonation, our bench scale tests
<strong>Ozone</strong> News Volume 37, No.3<br />
Figure 5. Plot showing impact of sludge ozonation on<br />
the incidence of filamentous bacterial species<br />
Figure 6. Effect of sludge ozonation on nitrogen<br />
removal. Solid black vertical line indicates<br />
commencement of sludge ozonation<br />
Table 3. Summary of results obtained during the pilot<br />
tests.<br />
suggested that the lysis products were sufficiently<br />
biodegradable and could be effectively removed in the<br />
aeration basin. Throughout the test period (May 2006 to<br />
March 2007) COD removal efficiency was maintained at<br />
the historical average of 80%. TN removal efficiency was<br />
also maintained at the historical pre-ozonation average<br />
level of 60% (See Figure 6 and Table 3). It is possible that<br />
the higher effluent COD levels that were observed in the<br />
Page 19<br />
effluent could have been due to the lack of supplemental<br />
oxygen to use in the bio-oxidation of the lysis products in<br />
the basin. It should be noted that the concentration of<br />
ozone in most generators would typically be in the range<br />
of 7-14% w/w <strong>Ozone</strong>, with the rest of the stream being<br />
made up of pure oxygen. While previous methods viewed<br />
this ‘excess oxygen’ stream as a waste gas, our approach<br />
permits the dissolution of this ‘excess oxygen’. There is<br />
sufficient oxygen in this stream to provide all of the<br />
supplemental oxygen required for the oxidation of the<br />
lysis COD products in the basin. During the pilot, the<br />
residual DO level in the basin went from a value of about<br />
1 mg/L to 2-3 mg/L following the commencement of the<br />
sludge ozonation process. It is conceivable that in<br />
addition to the benefits of reduced sludge handling and<br />
disposal costs, aeration power savings could be achieved<br />
in plants that have turn down capacity on their blowers<br />
based on the supplemental oxygen gains from the sludge<br />
ozonation process.<br />
The impact of sludge ozonation on excess sludge<br />
generation occurs rapidly and net changes in the trends<br />
for sludge generation can be observed within a few weeks<br />
of operations (Figure 7).<br />
Figure 7. Trends in cumulative excess sludge production,<br />
before (weeks 17-21) and after (weeks 21-30) partial<br />
sludge recycle ozonation.<br />
Conclusion<br />
Ozonation of sludge is an effective method for achieving<br />
a reduction in excess sludge generated in the activated<br />
sludge process. It is possible using a high selectivity<br />
reactor to achieve economical levels of ozone<br />
consumption that make sludge ozonation a commercial<br />
viable approach for sludge minimization.
<strong>Ozone</strong> News Volume 37, No.3<br />
Results from our study indicate that sludge ozonation had<br />
no effect on the nitrification efficiency during full scale<br />
applications (Vergine et al, 2007) confirming the<br />
observations of other groups (e.g., Lebrun et al (2006),<br />
Raugust & Schwerdt (2004)). Our studies indicate that<br />
the COD released during the lysis process is highly<br />
biodegradable.<br />
When optimally operated, the sludge ozonation process<br />
enables the realization of economical dosages and<br />
consumption levels of ozone in field tests. We did not<br />
observe a reduction in the COD and TN removal<br />
efficiencies at the plant, a result which was in agreement<br />
with the observations made at the bench scale regarding<br />
the very high biodegradability of the lysis products. Our<br />
experience also indicates that sludge ozonation can<br />
provide an effective means for biological foaming and<br />
bulking control in wastewater treatment operations.<br />
The sludge ozonation process has been successfully<br />
applied for sludge reduction at a municipal wastewater<br />
treatment plant that handles some textile wastewater as<br />
well. The following results have been obtained (i) Sludge<br />
reduction up to 60% (ii) Elimination of foaming<br />
problems (iii) Improvement in process stability (iv)<br />
Improvement of dewatering (v) Improvement of settling<br />
(vi) Improvement of effluent quality (vii) Effective COD<br />
removal.<br />
References<br />
1. Böhler M., Siegrist H. (2004) Partial ozonation of<br />
activated sludge to reduce excess sludge, improve<br />
denitrification and control scumming and bulking, Wat.<br />
Sci. Technol., 49(10), 41–49.<br />
2. Fabiyi, M & Novak, R (2007). System and method for<br />
eliminating sludge via ozonation. US Patent 7,3<strong>09</strong>,432.<br />
3. Kobayashi, T., Arakawa, K., Katu, Y., & Tanaka, T. (2001).<br />
Study on sludge reduction and other factors by use of an<br />
ozonation process in activated sludge treatment.<br />
Proceedings of 15th <strong>Ozone</strong> World Congress, London 2001,<br />
<strong>International</strong> <strong>Ozone</strong> Association, 321<br />
4. Perez-Elvira, S., Nieto Diez, P and Fdz-Polanco, F. (2006).<br />
Sludge Minimization Technologies. Reviews in<br />
Environmental Science and Biotechnology. Volume 5,<br />
Number 4 / November, 2006, pp 375-398<br />
5. Raugust G., Schwerdt J. (2004). 40% weniger –<br />
Reduzierung von Bioschlamm durch Ozonung.<br />
Verfahrenstechnik 38 (5) 16 - 17<br />
6. Ried et al. (2002). Optimierungsmöglichkeiten beim<br />
Betrieb von biologischen Kläranlagen durch den Einsatz<br />
von Ozon. Korrespondenz Abwasser 49 (5) 648-661<br />
Page 20<br />
7. Sakai et al. (1997). An activated sludge process without<br />
excess sludge production. Wat. Sci. Tech. 36 (11) 163-170<br />
8. Sievers et al. (2004). Sludge treatment by ozonation –<br />
Evaluation of full-scale results. Water Science &<br />
Technology Vol 49 No 4 pp 247 – 253<br />
9. Tchobanoglous, G., Burton, F., & Stensel, H. D (2003).<br />
Metcalf & Eddy Wastewater Engineering: Treatment and<br />
Reuse. McGraw Hill, NY.<br />
10. Vergine, P., Menin, G., Canziani, R., Ficara, E., Fabiyi, M.,<br />
Novak, R., Sandon, A., Bianchi, A., Bergna, G (2007).<br />
Partial Ozonation of Activated Sludge to Reduce Excess<br />
Sludge Production: Evaluation of Effects on Biomass<br />
Activity in a Full Scale Demonstration Test. IWA<br />
Conference, Moncton, Canada.<br />
11. WERF Report (2004). Evaluation of Feasibility of<br />
Methods to Minimize Biomass Production from<br />
Biotreatment.<br />
12. Yasui et al. (1996). A full-scale operation of a novel<br />
activated sludge process without excess sludge production.<br />
Wat. Sci. Tech. 34 (3-4) 395-404<br />
Praxair Sludge Ozonation Process
<strong>Ozone</strong> News Volume 37, No.3<br />
NEW IOA MEMBERS<br />
The <strong>International</strong> <strong>Ozone</strong> Asociation takes great pleasure in welcoming our new members<br />
BRAZIL<br />
Ericson Dalla<br />
Panozon Ambiental S/A<br />
Rua Dos Tuiuius, 654<br />
Piracicaba, SP 13.421-260<br />
Tel. +55 19-2105-2565<br />
Fax. +55 19-2105-2550<br />
dalla@tecnozon.com.br<br />
Carolina Kechinski<br />
356 Alcebiades Antonio dos Santos<br />
Rio Grande do Sul<br />
Tel. +55 55-51-3737-37<br />
carolpk@eng.ufrgs.br<br />
CANADA<br />
Dave Montgomery<br />
Trow Associates, Inc.<br />
1595 Clark Boulevard<br />
Brampton, ON L6T 4V1<br />
dave.montgomery@trow.com<br />
CZECH REPUBLIC<br />
Mrs. Marketa KOPECKA<br />
Ingersoll Rand Equipment Manufacturing<br />
Czech Republic s.r.o.<br />
R&D Center Prague<br />
Florianova 2460<br />
253 01 Hostivice<br />
Tel. +420 257 1<strong>09</strong> 782<br />
Fax. +420 251 562 187<br />
Marketa_Kopecka@eu.irco.com<br />
FRANCE<br />
M. Frédérick COUSIN<br />
DEGRÉMONT<br />
23-25 avenue de la République<br />
92508 RUEIL-MALMAISON<br />
Tel. +33 146 253 970<br />
Fax. +33 146 253 955<br />
frederick.cousin@degremont.com<br />
JAPAN<br />
Mr. Norihito Asah<br />
ExecutiveManaging Director<br />
Toyashima Denki co.Ltd.<br />
1- 391 Komaki Komakio City<br />
Aichi Pref. 485-0041<br />
Tel. + 81-568-72-5590<br />
Fax. + 81-568-72-5590<br />
Dr. Douyan Wang<br />
Assistant Professor<br />
Priority organization for Innovation and<br />
Excellence<br />
Kumamoto University<br />
2-39-1 Kurokami<br />
Kumamoto 860-8555<br />
Tel. +81-96-339-1445<br />
Fax. +81-96-339-1445<br />
douyan@kumamoto-u.ac.jp<br />
MEXICO<br />
Clementina Ramirez C.<br />
Universidad Autónoma Metropolitana<br />
San Pablo 180<br />
Col Reynosa Tamaulipa<br />
Delegacion Azcapotzalco<br />
Mexico, DF 02200<br />
Tel. +52 55-5318-9044<br />
crrc@correo.azc.unam.mx<br />
P.R. OF CHINA<br />
Prof. Jun MA<br />
Harbin Institute of Technology<br />
PO Box 2627<br />
202 Haihe Road<br />
HARBIN 150<strong>09</strong>0<br />
Tel. +86 4516282292<br />
Fax. +86 4512368074<br />
majunhit@gmail.com<br />
Page 21<br />
SPAIN<br />
Mr. Bruno DOMENJOUD<br />
C/Londres, 1, 2º-3ª<br />
08029 BARCELONA<br />
Tel. +34 934 039 789<br />
b.domenjoud@angel.qui.ub.es<br />
TURKEY<br />
Ms. Leman GÜLER<br />
Ege Ticaret Merkezi 1202/1<br />
Sak No: 29/1-C Kati 1<br />
Kenisehi<br />
IZMIR<br />
Tel. +90 536 968 62 07<br />
Fax. +90 232 457 6166<br />
lemanguler@gmail.com<br />
UNITED STATES OF AMERICA<br />
Mr. Tom Birchard<br />
Ingersoll Rand Equipment Climate<br />
Control Technologies<br />
Thermo King Corp.<br />
314 West, 90th Street Minneapolis<br />
MN 55420<br />
Tel. +1 952 887 2323<br />
Fax. +1 952 885 3506<br />
tom_birchard@irco.com<br />
Don Finnegan<br />
Fin-Tek Corporation<br />
6 Leo Place<br />
Wayne, NJ 07470<br />
Tel. 862-368-4122<br />
don@fin-tek.com<br />
Raghu Gummaraju<br />
BASF Catalysts LLC<br />
25 Middlesex/Essex Turnpike<br />
Iselin, NJ 08830<br />
Tel. 732-205-5481<br />
Fax. 734-626-1217<br />
raghu.gummaraju@basf.com
<strong>Ozone</strong> News Volume 37, No.3<br />
Don Finnegan<br />
Fin-Tek Corporation<br />
6 Leo Place<br />
Wayne, NJ 07470<br />
Tel. 862-368-4122<br />
don@fin-tek.com<br />
Raghu Gummaraju<br />
BASF Catalysts LLC<br />
25 Middlesex/Essex Turnpike<br />
Iselin, NJ 08830<br />
Tel. 732-205-5481<br />
Fax. 734-626-1217<br />
raghu.gummaraju@basf.com<br />
David Johnson<br />
Fin-Tek Corporation<br />
6 Leo Place<br />
Wayne, NJ 07470<br />
Tel. 862-368-4122<br />
dave@fin-tek.com<br />
New IOA Members, Cont’d)<br />
Perry Johnson<br />
AE3S<br />
2106 S. Washington St.<br />
Grand Forks, ND 58201<br />
Tel. 701-746-8087<br />
perry.johnson@ae2s.com<br />
Richard Lin<br />
MWH Global Inc.<br />
PO Box 443<br />
Temple City, CA 91780<br />
Tel. 626-318-2326<br />
richard.lin@mwhglobal.com<br />
Joseph Manzo<br />
BrainPad<br />
322 Fayette St.<br />
Conshohocken, PA 19428<br />
jmanzo@brainpad.com<br />
Walter Meuse<br />
Portland Water District<br />
2 White Rock Rd<br />
Standish, ME 04084<br />
Tel. 207-774-5961<br />
wmeuse@pwd.org<br />
Andrew Posner<br />
83 Rogers St.<br />
Cambridge, MA 02142<br />
Tel. 617-354-6100<br />
aposner@joulebio.com<br />
More scenes from Cambridge Conference<br />
Page 22<br />
Mickey Walsh<br />
Fin-Tek Corporation<br />
6142 Colquitt Road<br />
Keithville, LA 71047<br />
Tel. 973-988-1086<br />
mickey@fin-tek.com<br />
Christopher Waters<br />
CDM<br />
1715 N Westshore Dr., Suite 875<br />
Tampa, FL 33607<br />
Tel. 813-281-2900<br />
waterscj@cdm.com<br />
Ed Williams<br />
CF Design<br />
650 Peter Jefferson Place, Suite 250<br />
Charlottesville, VA 22911<br />
Tel. 434-977-2764<br />
ed.williams@cfdesign.com<br />
Andrew Wright<br />
IN USA Inc.<br />
100 Morse St.<br />
Norwood, MA 02062<br />
Tel. 781-444-2929<br />
awaright@inusacorp.com
<strong>Ozone</strong> News Volume 37, No.3<br />
Upcoming IOA Meetings<br />
August 31- September 2, 20<strong>09</strong>, 19th <strong>Ozone</strong> World<br />
Congress, Tower Hall Funabori (Tokyo) Japan. The<br />
congress will end with a technical/sightseeing tour to<br />
Kyoto.<br />
Topics will include:<br />
• Disinfection<br />
• Chemical and Biochemical Reactions<br />
• Air Treatment<br />
• Bromate Formation and Control<br />
• <strong>Ozone</strong> Generation/Contacting<br />
• Advanced Oxidation<br />
• Small ozonation systems<br />
• UV technologies/ Reactor design/validation<br />
• Medical Applications<br />
• Cooling Tower Applications<br />
• Food and Agricultural Applications<br />
• Spa/Pool/Aquarium<br />
• Industrial Applications<br />
• Water and Wastewater Treatment<br />
• Emerging Contaminants<br />
For more information, contact: Japan Association at<br />
joa@mwd.biglobe.ne.jp or visit websites www.io3a.org,<br />
www. ioa-ea3g.org or www.j-ozone.org (in Japanese).<br />
Detailed information on the conference is included in this<br />
issue.<br />
2010<br />
April 28-30, 2010, IOA-EA3G <strong>International</strong> Conference,<br />
Geneva, Switzerland: “Emerging parameters in water and<br />
environment: Benefits of ozone and other oxidants”. The<br />
conference will focus on potable water treatment;<br />
wastewater, domestic, mixed domestic-industrial;<br />
industrial wastewater and biological sludge treatment.<br />
Emphasis will be on micropollutants elimination. For<br />
more information, contact Ms. Béatrice Bernard,<br />
Secretariat IOA-EA3G: ioa@esip.univ-poitiers.fr or visit<br />
www.ioa-ea3g.org.<br />
Meetings Calendar<br />
Page 23<br />
September 20-22, 2010, Pan American Group Regional<br />
Conference,Hyatt Regency, Bellevue (Seattle). WA,<br />
USA.<br />
2011<br />
2011, 20th <strong>Ozone</strong> World Congress, Paris France. More<br />
information will be forthcoming after the 20<strong>09</strong> World<br />
Congress. Information: www.io3a.org.<br />
Upcoming Meetings of Other Organizations<br />
20<strong>09</strong><br />
August 16-22,20<strong>09</strong>, World Water Week 20<strong>09</strong>, Stockholm<br />
Sweden. Information: www.worldwaterweek.org<br />
August 26-29, 20<strong>09</strong>, Association of Water Technologies<br />
Annual Convention and Exposition, Hollywood, FL.<br />
Information: www.awt.org<br />
September 6-9, 20<strong>09</strong>, First IWA Development Congress,<br />
Mexico City, Mexico. Information:<br />
www.iwa20<strong>09</strong>mexico.org<br />
September 14-15, 20<strong>09</strong>, 1st <strong>International</strong> Workshop on<br />
Application of Redox Technolgies in the Environment,<br />
Istanbul Technical University, Istanbul, Turkey. The<br />
workshop aims at providing a unique platform for the<br />
presentation and discussion of the state-of-the-art as well<br />
as latest developments concerning the application of<br />
environmental redox technologies for the treatment of<br />
water and wastewater. Presentations will focus on<br />
drinking water treatment, industrial wastewater<br />
treatment, domestic wastewater treatment and emerging<br />
treatment technologies. For more information, visit the<br />
conference website www.aarate20<strong>09</strong>.itu.edu.tr or contact<br />
the organizing committee, Prof. Miray Bekbolet at<br />
bekbolet@boun.edu.tr.
<strong>Ozone</strong> News Volume 37, No.3<br />
Meetings (cont’d)<br />
September 17-18, 20<strong>09</strong>, Ultrapure Water – Pharma,<br />
East Brunswick, NJ, USA. Information:<br />
www.ultrapurewater.com<br />
September 20-25, 20<strong>09</strong>, 7th IWA World Congress on<br />
Water Reclamation and Reuse, Brisbane, Australia.<br />
Information: www.reuse<strong>09</strong>.org<br />
September 21-23, 20<strong>09</strong>, 5th World Congress on<br />
Ultraviolet Technology, Amsterdam, The Netherlands.<br />
Infromation: www.iuva.org<br />
October 4-9, 20<strong>09</strong>, 20<strong>09</strong> <strong>International</strong> Water<br />
Conference, Orlando, FL. Information: www.eswp.com<br />
October 10-14, 20<strong>09</strong>, WEFTEC<strong>09</strong> 82nd Annual<br />
Technical Expostion and Conference, Orange County<br />
Convetnion Center, Orlando, FL. Information:<br />
www.weftec.org<br />
October 28-30, 20<strong>09</strong>, 20<strong>09</strong> World Aquatic Health<br />
Conference, “Healthy Pools, Healthy Bodies”, Sheraton<br />
Atlanta Hotel, Atlanta, GA. This conference, hosted by<br />
the National Swimming Pool Foundation® is in<br />
partnership with the National Environmental Public<br />
Health Conference (NEPHC) organized by the Centers<br />
for Disease Control. For more information:<br />
www.nspf.org.<br />
November 10-13, 20<strong>09</strong>, Aqua Ukraine 20<strong>09</strong>, Kiev,<br />
Ukraine. Information: www.tech-expo.com.ua<br />
November 13-18, 20<strong>09</strong>, <strong>International</strong> Pool| Spa| Patio<br />
Expo, Las Vegas, NV, USA. Information:<br />
www.PoolSpaPatio.com<br />
November 15-19, 20<strong>09</strong>, AWWA Water Quality<br />
Technology Conference & Exposition, Sheraton at<br />
Washington State Convention Center, Seattle WA.<br />
Information: www.awwwa.org.<br />
2010<br />
March 8-10, 2010, OZWater’10, Brisbane, Australia.<br />
Information: www.ozwater10.com.au<br />
Page 24<br />
March 9-12, 2010. WQA Aquatech USA, Orlando, FL.<br />
Information: www.wqa.org<br />
June 20-24, 2010, ACE10: AWWA Annual Conference &<br />
Exhibition, Chicago, IL. Information: www.awwa.org<br />
June 28-July 1, 2010, 6th <strong>International</strong> Symposium on<br />
<strong>Ozone</strong> Applications and 5th <strong>International</strong> Symposium on<br />
Environment, <strong>International</strong> Convention Center, Havana<br />
Cuba. Topics will consider <strong>Ozone</strong> Experimental<br />
Medicine and Medical Treatments; <strong>Ozone</strong> Chemistry;<br />
Ozonized Vegetable Oils; <strong>Ozone</strong> in Food Industry;<br />
Treatment of Water, Wastewater and Solid Wastes;<br />
Environmental Management; Renewable Energy and<br />
<strong>Ozone</strong> Generation System Design. Call for papers:<br />
Abstracts due March 31, 2010. For more information:<br />
visit www.ozono.cubaweb.cu or email<br />
silviamenendez@infomed.sld.cu.
<strong>Ozone</strong> News Volume 37, No.3<br />
FIRST ANNOUNCEMENT<br />
6 th INTERNATIONAL SYMPOSIUM ON OZONE APPLICATIONS AND<br />
V INTERNATIONAL SYMPOSIUM ON ENVIRONMENT<br />
Dear colleagues:<br />
The <strong>Ozone</strong> Research Center of Cuba is pleased to invite you to take part in the 6th <strong>International</strong><br />
Symposium on <strong>Ozone</strong> Applications and V <strong>International</strong> Symposium on Environment.<br />
The symposium will be held in the “<strong>International</strong> Convention Center” at Havana City from June 28th<br />
through July 1st, 2010, within the framework of the 15 th <strong>International</strong> Scientific Congress CNIC<br />
2010.<br />
The aim of this Symposium is to offer an appropriate and fruitful framework for sharing experiences,<br />
scientific ideas and addressing current advances in the use of ozone and the environmental subjects. All<br />
this will contribute to strengthen even more our ties of friendship and cooperation. For this reason, we<br />
invite all specialists, from all over the world, to present their papers in this congress or to participate only<br />
as delegates.<br />
A broad scientific program has been organized with the topics tackled at present by our Center as well as<br />
those developed in collaboration with other Cuban institutions during these 30 years of scientific work.<br />
The main subjects in the Symposium will be: <strong>Ozone</strong> Experimental Medicine and Medical<br />
Treatments; <strong>Ozone</strong> Chemistry; Ozonized Vegetable Oils; <strong>Ozone</strong> in Food Industry; Treatment of<br />
Water, Waste Water and Solid Wastes; Environmental Management; Renewable Energy and<br />
<strong>Ozone</strong> Generation System Design.<br />
All work sessions will comprise lectures, oral presentations and posters (75 x 120 cm).<br />
With the aim to achieve a broad promotion of the papers, persons that are interested to participate must<br />
submit abstracts (with no more than 250 words) in English language, which includes the title of the<br />
paper, author's name(s), institution, city and country where the work was carried out. The author who<br />
presents the work should be marked with an asterisk (*). The deadline<br />
for the presentation of the abstracts will be March 31 ST , 2010.<br />
Participants will pay a registration fee of 350.00 CUC (it includes a<br />
CD-ROM with the Symposium Proceedings, participation in all scientific<br />
sessions and farewell cocktail) and accompanied persons 100.00 CUC<br />
(it includes participation in the farewell cocktail).<br />
The official languages will be Spanish and English.<br />
We hope the Caribbean warmth, which characterizes our country,<br />
welcomes you in a nice, relaxing and beautiful environment like the one offered by the “<strong>International</strong><br />
Convention Center”, located on the west of Havana, just a few minutes from the center of the city. The<br />
climate of our country, the security that it offers and the traditional hospitality of the Cuban people<br />
contribute to convert the <strong>International</strong> Convention Center of Havana in a suitable place for the<br />
celebration of our event.<br />
Please in order to obtain more details about the event contact to:<br />
Dr. Lidia Asela Fernández<br />
President<br />
Dr. Silvia Menéndez Cepero<br />
Organizing Secretary<br />
<strong>Ozone</strong> Research Center, Calle 230 No. 1313 esq. Avenida 15, Siboney, Playa,<br />
Apartado Postal 6412, Ciudad de La Habana, Cuba.<br />
Phone: (53-7) 271-2089, 271-9264,<br />
Fax: (53-7) 271-0233<br />
E-mail: simposio@cnic.edu.cu; silviamenendez@infomed.sld.cu;<br />
Website: http://www.ozono.cubaweb.cu; http://ozonocanada.cubaweb.cu; www.congresocniccuba.com<br />
Page 25
<strong>Ozone</strong> News Volume 37, No.3<br />
19 th World Congress & Exhibition, Tokyo, Japan<br />
<strong>International</strong> <strong>Ozone</strong> Association<br />
31 August - 3 September 20<strong>09</strong><br />
Tower Hall Funabori, Funabori, Edogawa-ku, Tokyo, Japan<br />
(draft)<br />
Preliminary Congress Description<br />
� � � � � � � � � �<br />
1. Purpose<br />
Today, throughout the world, ozonation technologies have been widely used to establish the safe and comfortable life<br />
and production process in high-technology industry. This is because ozone has a strong oxidation capacity, no harmful<br />
residues after its decomposition, easy management and control characteristics. Accordingly, the ozonation technologies<br />
are greatly expected to play an important role in a wide variety of industries in future.<br />
Meanwhile, in Japan, ozonation technologies have been also widely used to get tasty and safe drinking water, and<br />
expected to be improved for more effective and new capacity in water purification plants. Gradually, they have been<br />
also applied to spa, pool and aquarium for clear water, agriculture, food and beverage for disinfection and high<br />
technology production plant for clean-up. Additionally, they are expected to be adopted more in sewage and wastewater<br />
treatment field for water environment preservation and reuse of the treated wastewater.<br />
The <strong>Ozone</strong> World Congress is held biennially, where researchers, engineers, consultants, and people concerned gather<br />
from all over the world for presentations and discussions of the results from their researches and experiences. Through<br />
the <strong>Ozone</strong> World Congress, all participants can get up-to-date information, knowledge and innovative ideas, surely<br />
contributing to the development of ozone science and technology.<br />
It will be the third time for Japan to hold the <strong>Ozone</strong> World Congress in 20<strong>09</strong>, including the 7 th congress (Tokyo, 1985)<br />
and the 13 th congress (Kyoto, 1997). This congress should be a good opportunity to get up-to-date information of the<br />
science and technology developed in Japan as well as all over the world.<br />
2. Topics Included<br />
Main topics included in this congress are as follows;<br />
Disinfection Small Ozonation Systems<br />
Chemical and Biochemical Reactions Cooling Tower Applications<br />
Water Treatment Food and Agricultural Applications<br />
Waste Water Treatment Spa/Pool/Aquarium<br />
Air Treatment Industrial Applications<br />
Bromate Formation and Control UV technologies<br />
Emerging Contaminants UV Reactor design/validation<br />
<strong>Ozone</strong> Generation/Contacting Medical Applications<br />
Advanced Oxidation<br />
3. Schedules of the Congress & Exhibition<br />
Morning<br />
Afternoon<br />
Monday<br />
31 Aug. 20<strong>09</strong><br />
Registration<br />
Exhibition<br />
Evening Welcome<br />
reception<br />
Tuesday<br />
1 Sep. 20<strong>09</strong><br />
Welcome &<br />
Preliminary Session<br />
Oral & poster<br />
presentation,<br />
Exhibition<br />
Technical tour<br />
Wednesday<br />
2 Sep. 20<strong>09</strong><br />
Oral & poster<br />
presentation,<br />
Exhibition<br />
Oral & poster<br />
presentation,<br />
Exhibition<br />
Technical tour<br />
Page 26<br />
Thursday<br />
3 Sep. 20<strong>09</strong><br />
Oral & poster<br />
presentation,<br />
Exhibition<br />
Oral & poster<br />
presentation<br />
Gala night<br />
Friday<br />
4-5 Sep. 20<strong>09</strong><br />
Special Technical<br />
Social tour<br />
(Over night to Kyoto)<br />
4. Technical tour (option)<br />
Technical tour to visit ozone application facilities including the Asaka Water Purification Plant and the Shibaura<br />
reclamation Plant in Tokyo area will be prepared in the afternoon on Sep. 1 and 2, 20<strong>09</strong>.<br />
5. Special technical tour (option)<br />
2 days special tour on Sept. 4 and 5, 20<strong>09</strong>, to visit water and wastewater treatment plants in Kyoto Area will be
<strong>Ozone</strong> News Volume 37, No.3<br />
prepared. You can enjoy comfortable Super Express Train “Shinkansen” and historical Kyoto City.<br />
6. Social tour (option)<br />
Several social programs will be also prepared. You can enjoy Japanese historical, traditional and nice sightseeing<br />
spots.<br />
7. Registration<br />
Registration fees are shown in the following table<br />
Early bird registration Regular registration<br />
Before May 31, 20<strong>09</strong> after June 1 st , 20<strong>09</strong><br />
Technical session<br />
(including proceedings, exhibits<br />
& opening reception)<br />
IOA, JOA members<br />
Non members<br />
Students<br />
45,000 JPY<br />
55,000 JPY<br />
10,000 JPY<br />
50,000 JPY<br />
60,000 JPY<br />
10,000 JPY<br />
Gala night<br />
Accompanying person<br />
10,000 JPY 15,000 JPY<br />
(Welcome reception, Welcome & Preliminary Session,<br />
Exhibits and Gala night )<br />
15,000 JPY 20,000 JPY<br />
Technical tour 6,000JPY 6,000JPY<br />
Special technical tour 50,000JPY 50,000JPY<br />
Social tour option option<br />
Visit: https://apollon.nta.co.jp/ozone20<strong>09</strong>-er/ IOA WC20<strong>09</strong> Desk Nippon Travel Agency Co .,Ltd<br />
TEL:81-3-5565-9895, FAX 81-3-5565-9899<br />
8 Hotel Accommodation visit: https://apollon.nta.co.jp//ozone20<strong>09</strong>-eh/<br />
9. Preliminary Technical Program (Tentative on April 1)<br />
IOA <strong>International</strong> congress in 20<strong>09</strong><br />
�<br />
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am�<br />
9:00�<br />
-12:05�<br />
pm�<br />
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-6:30�<br />
Sept. 1�<br />
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Room 1 Room 2 Room 3� Room 1 Room 2 Room 3<br />
Opening�<br />
Ceremony�<br />
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Simultaneous Translation will be<br />
prepared in Room 1. �<br />
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Room 4 Room 5�<br />
Medical � �7��<br />
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Session �<br />
�13��<br />
Page 27<br />
��Sept. 3�<br />
Room 1 Room 2 Room 3�<br />
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Sept. 3�<br />
Room 4�<br />
Medical�<br />
Session�<br />
�<br />
Medical�<br />
Session�<br />
�<br />
�Water Purification: Session �1� �<strong>Ozone</strong> Solubilization and Decomposition: Session �13� �<br />
�Emerginng Contaminants: Session �2� �Sludge Treatment: Session �14� �<br />
�Industrial Application: Sessions �3�&�11� �Air and Gas Treatment: Session �15�<br />
�Municipal Wastewater Treatment: Sessions �4�&�8� �Industrial Wastewater Treatment: Sessions �16�<br />
&�19� �<br />
�Advanced Oxidation Process: Sessions �5�&�9� ���: Session �17� �<br />
�Byproducts and Control: Session �6� �Disinfection: Session �18� �<br />
�<strong>Ozone</strong> Generation: Sessions �7�&�12��Medical Application Session Medical �<br />
�Agriculture-food-beverage application: Session �10� �
<strong>Ozone</strong> News Volume 37, No.3<br />
Presentation Programmee (Tentative on April 1)<br />
�<br />
This programmee is tentatively made for associated persons to understand presentation contents.�<br />
The presentation date and time and order of each paper will be changed because only persons who register with<br />
registration fee before May 31 can present and be recorded in the final programmee.�<br />
�<br />
Sept. 1 (Tuesday) p.m.(13:30-18:30)��<br />
�<br />
Session �17� at Room� ��<br />
��� �Oguma��<br />
Key note speech�<br />
145 UV treatment of water in Japan; applications, situations and developments�<br />
� ���Ritsumeikan University Naoyuki Kamiko Japan�<br />
General presentation�<br />
24 UV/TiO2 for Removing Taste and Odour Compounds in Drinking Water: Influence of Water Composition<br />
and Destruction Mechanism �<br />
School of Engineering, The University of Newcastle Hoang N Tran Australia�<br />
38 Investigation of generation mechanisms of nitrite in UV irradiation�<br />
Department of Integrated Science and Engineering, Graduate School of Science and Engineering,<br />
Ritsumeikan University Nobuhito YASUI Japan�<br />
39 Hydraulic optimization of a single UV lamp placed perpendicular to the flow direction�<br />
B.A. Wols�<br />
48 Research on the Actinometer Corresponding to High Dose Range�<br />
Iwasaki Electric � �Yuuko Hiroto Japan�<br />
56 Distribution characteristics of light source in ultraciolet band�<br />
Japan Photo-Science Yuji Yamakoshi�<br />
58 Photo-transformation of amoxicillin during UV treatment and toxicological assessment of its intermediates�<br />
Department of Environmental Engineering, Yonsei University�<br />
Joon-Wun Kang Korea�<br />
60 Growth inhibition of indigenous Microcystis species in a lake using a medium-pressure UV treatment<br />
system�<br />
Dept. of Urban Engineering, The University of Tokyo Hiroshi SAKAI Japan�<br />
121 MELBOURNE WATER�S APPROACH TO ONE OF THE WORLD�S MOST COMPLEX<br />
WASTEWATER TECHNOLOGY TRIALS�<br />
Melbourne Water Corporation Mark Lynch Ausyralia�<br />
�<br />
�<br />
�<br />
Session �2� at Room� ��<br />
�Emerginng Contaminants �Suzuki, Ikehata��<br />
Key note speech�<br />
122� Role of ozonation in the destruction of EDCs and Pharmaceuticals� ��<br />
Applied R & D Center Shane Snyder USA�<br />
61 Application of O3 and O3/UV processes for the removal of PPCPs in secondary treated water: �<br />
Energy consumption for the rffrctive PPCPs removal Kyoto University Iiho Kim Japan�<br />
General presentation�<br />
2 Removal of Bisphenol A from aqueous solution by ozonation�<br />
San Diego State University Temesgen Garoma USA�<br />
101 Removal Characteristics of EDCs by Ozonation�<br />
Graduate School of Engineering, Kyoto University Hiroshi TSUNO Japan�<br />
35 Perovskite catalytic ozonation of some pharmaceutical compounds in water�<br />
Departamento de Ingeniería Química y Química Física. Universidad de Extremadura�<br />
P. Pocostales Spain�<br />
88 REMOVAL OF PROPRANOLOL IN AQUEOUS PHASE BY OZONATION�<br />
Departament d�Enginyeria Química, Universitat de Barcelona. Renato F. Dantas�<br />
127 REMOVAL OF ENDOCRINE DISRUPTING COMPOUNDS �EDCS� AND �<br />
PHARMACEUTICALS AND PERSONAL CARE PRODUCTS �PPCPS� FROM DRINKING WATER<br />
USING ADVANCED OXIDATION PROCESS�<br />
Page 28
<strong>Ozone</strong> News Volume 37, No.3<br />
Dept. of Civil and Environmental Engineering, University of Western Ontario M.F. Rahman Canada�<br />
22 PEROXIDATION OF CHLOROPHENOLS IN SOIL�<br />
Department of Chemical Engineering, Tallinn University of Technology Anna Goi Estonia�<br />
�<br />
Session �3� at Room� ��<br />
�Industrial Application �Kuzumoto, Nishijima, Lezmik, Liechti��<br />
Key note speech�<br />
73 <strong>Ozone</strong>: Science & engineering 30 yeras of progress�<br />
<strong>Ozone</strong> science & engineering � Barry L. Loeb USA�<br />
General presentation�<br />
8 Direct Plasma Degradation of Perfluorooctanoic Acid in Gas-Liquid Two-Phase Flow Reactor�<br />
Dept. of Electrical and Electronic Eng.,Tokyo Institute of Technology K. Sasaki Japan�<br />
9 Decomposing Mechanisms of Persistent Organics in Water Using Direct Plasma Method �<br />
Dept. of Electrical and Electronic Eng., Tokyo Institute of Technology Koichi Yasuoka Japan�<br />
16 THE OZONE LAUNDRY HANDBOOK A Comprehensive Guide for the Proper Application of<br />
<strong>Ozone</strong> in the Commercial Laundry Industry�<br />
RICE <strong>International</strong> Consulting Enterprises Rip G. Rice USA�<br />
15 ECONOMIC AND ENVIRONMENTAL BENEFITS OF OZONE IN OZONE LAUNDERING<br />
SYSTEMS�<br />
RICE <strong>International</strong> Consulting Enterprises Rip G. Rice USA�<br />
17 MICROBIOLOGICAL BENEFITS OF OZONE IN OZONE LAUNDERING SYSTEMS�<br />
RICE <strong>International</strong> Consulting Enterprises Rip G. Rice USA�<br />
20 <strong>Ozone</strong> application for chamois leather making�<br />
Dr.Mahalingam College of Engineering and Technology V.Lakshminarayanan India�<br />
21 Two tone leathers using <strong>Ozone</strong>�<br />
Dr.Mahalingam College of Engineering and Technology V.Lakshminarayanan India�<br />
44 Super-hydrophilization of Stainless Steel Surface by the Combined Use of Gaseous <strong>Ozone</strong> and Heat�<br />
Food & Bio-technology Group, Industrial Technology Center of Okayama Prefecture�<br />
Kazuhiro Takahashi Japan�<br />
59 Densification of CVD-SiO2 film using high-density ozone treatment�<br />
Advanced Technology R&D Center, Mitsubishi Electric Corporation �<br />
Kazumasa KAWASE Japan<br />
�<br />
�<br />
Sept. 2 (Wednesday) p.m.(9:00-12:05)��<br />
�<br />
Session �4� at Room� ��<br />
�Municipal Wastewater Treatment �Murakami, Thompson��<br />
Key note speech�<br />
111 State of ozonation to municipal wastewater treatment in Japan�<br />
Japan Sewage Works Agency Toshikazu Hashimoto Japan�<br />
23 <strong>Ozone</strong> treatment of secondary effluent at US municipal wastewater treatment plants�<br />
MWH Americas Michael A. Oneby USA�<br />
General presentation�<br />
67 The potential use of ozone in municipal waste water�<br />
ITT-WWW WEDECO A. Ried Germany�<br />
89 Ozonation of municipal secondary effluent �<br />
Chemical Engineering Dpt, University of Barcelona B. Domenjoud Spain�<br />
137 Treatment efficiency and operational parameter of ozonation of secondary effluent�<br />
JOA Hirofumi Takahara Japan�<br />
128 Development of Ultra-advanced Sewage Treatment by Compound Oxidation using Advanced Oxidation<br />
Process�<br />
TAKUMA Co. Ltd. Tomoyuki Doi Japan�<br />
32 Demonstration research of micro-bubbling system of ozone for reuse of treated sewage�<br />
Hitachi Misaki Sumikura Japan�<br />
�<br />
Session �5� at Room� ��<br />
�Advanced Oxidation Process �Nakayama, Adams��<br />
Key Note Speech�<br />
Page 29
<strong>Ozone</strong> News Volume 37, No.3<br />
138 Review and perspective in application of advanced oxidation process �<br />
���������JOA Shigeki Nakayama Japan�<br />
General presentation�<br />
26 The investigation of ozone/hydrogen peroxide treatment after coagulation and edimentation in drinking<br />
water plant�<br />
Mitsubishi Electric Corporation N. Yasunaga Japan�<br />
29 Simultaneous Control of Bromate Ion and Chlorinous Odor in Drinking Water using Advanced<br />
Oxidation Processes �O3/H2O2��<br />
Department of Urban Management, Graduate School of Engineering, Kyoto University�<br />
Songkeart Phattarapattamawong Japan�<br />
100 O3/H2O2 process for both removal of odors and control of bromate ion formation�<br />
Department of Urban and Environmental Engineering, Graduate School of EngineeringKyoto University�<br />
Shinya Ohara Japan�<br />
68 Advanced Oxidation Process – effective and technical suitable for Micropollutant Removal in<br />
contaminated Water Sources�<br />
ITT-WEDECO GmbH Dr Achim Ried Germany�<br />
40 Diclofenac removal by UV and UVA/O3 processes�<br />
Departamento de Ingeniería Química y Química Física.Universidad de Extremadura�<br />
Juan F. García-Araya Spain�<br />
49 Effects of addition of hydrogen peroxide and/or calcium carbonate on ozone-decomposition of phenol or<br />
chlorophenol sparingly dissolved in water�<br />
Department of Chemical, Energy and Environmental Engineering Kansai University�<br />
Katsuhiko Muroyama Japan�<br />
135 A new catalyzed ozone process on water treatment �<br />
Applied Catalyst Tech. S.-J. Lin Taiwan�<br />
�<br />
Session �6� at Room� ��<br />
�Byproducts and Control �Kosaka, Dimitriou��<br />
Key note speech�<br />
1<strong>09</strong> Results of the AWWARF IOA bromateresearch project�<br />
Jacobs Engineering Michael Dimitriou� �USA�<br />
139 Ozonation byproducts in Japan Kyoto University Shinya Echigo Japan�<br />
General presentation�<br />
123 Decomposition of bromate by biological activated carbon�<br />
State Key Laboratory of Environmental Aquatic Chemistry, Research Center for Eco-Environmental<br />
Sciences, Chinese Academy of Sciences �<br />
Min Yang China�<br />
102 Behaviors of halogenated compounds during pre-chlorine, ozone and post-chlorine treatment�<br />
Graduate School of Engineering, Kyoto University Eri Hasegawa Japan�<br />
30 An Australian Perspective of <strong>Ozone</strong>/BAC Process for Reducing Disinfection By-product Precursors in<br />
Organics-laden Water�<br />
Hunter Water Australia Pty Ltd Yaode Yan Australia�<br />
5 Toxicity and Formation of Oxidation Byproducts Generated during Ozonation of�<br />
Natural Water Containing Pesticide�<br />
University of Alberta Pamela Chelme-Ayala Canada�<br />
72 Identification of N-nitrosodimethylamine precursors by ozonation from influent of a sewage treatment<br />
plant�<br />
Department of Water Supply Engineering, National Institute of Public Health�<br />
Koji Kosaka Japan�<br />
124 Formation of aldehydes formed during ozonation of secondary effluent from a sewage treatment plant and<br />
their ecological effect�<br />
State Key Laboratory of Environmental Aquatic Chemistry, Research Center for Eco-Environmental<br />
Sciences, Chinese Academy of Sciences�<br />
Min Yang China�<br />
�<br />
Session �7� at Room� ��<br />
�<strong>Ozone</strong> Generation �Ito, ��<br />
Key note speech�<br />
140 State of the art of ozone generation technologies in Japan�<br />
Chiba Institute of Technology Haruo Ito� ���Japan�<br />
Page 30
<strong>Ozone</strong> News Volume 37, No.3<br />
Page 31
<strong>Ozone</strong> News Volume 37, No.3<br />
<strong>Ozone</strong> Research Center. Nacional Center of Scientific Research Eliet Véliz Lorenzo Cuba�<br />
118 The Enhancement of Permeation Efficiency in Ceramic Membrane Bio-reactor by <strong>Ozone</strong>�<br />
Environmental Research and Management Center, Hiroshima University T.-Y. Tsai Japan�<br />
120 Treated Water Quality Enhancements from Ozonation/Biologically Active Filtration in a Tertiary Plant<br />
Upgrade�<br />
Melbourne Water Corporation John Mieog Australia�<br />
125 Treatment Characteristics of Wastewater Containing Phenol and Reaction Mechanism by <strong>Ozone</strong>-Added<br />
Activated Sludge Process�<br />
Dept. of Urban and Environmental Engineering, Kyoto University �<br />
Fumitake NISHIMURA Japan�<br />
81 Updating an Existing Wastewater Ozonation System with Generators and Sidestream Injection�<br />
� Black & Veatch Jeff Neemann USA�<br />
108 Application examples of ozonation for reuse of treated sewage in Tokyo�<br />
Sewage Works Bureau of Tokyo Yoshitake Yoda Japan�<br />
126 Installation and operation of full-scale ozonation facility to sewage treatment plants in Kyoto City�<br />
Director , Fushimi Wastewater Treatment Plant Water and Sewage Works Bureau of Kyoto City�<br />
Haruki Mizutani Japan�<br />
141 Super advanced treatment with ozone and BAC in Lake Biwa basin-wide Sewage system�<br />
Shiga Prefecture S.Nishimura Japan�<br />
Poster presentation�<br />
142 Reuse of treated sewage by application of ozone in Yokohama City�<br />
Yokohama City Japan �<br />
�<br />
�<br />
Session �9� at Room� ��<br />
�Advanced oxidation process �Nakayama, Adams��<br />
General� presentation�<br />
51 THE ADVANCED OXIDATION PROCESSES WITH OZONE, OZONE-UV, AND OZONE-UV.H2O2<br />
AN ALTERNATIVE FOR TREATMENT OF 2,5-DICHLOROPHENOL.�<br />
Universidad Autónoma Metropolitana – Azcapotzalco Ramírez-Cortina Clementina R. Mexico�<br />
52 PHYTOTOXICITY OF INTERMEDIATE COMPOUNDS OF PHENOL OXIDATION WITH OZONE<br />
AND OZONE-UV�<br />
� Universidad Autónoma Metropolitana-Azcapotzalco Ramírez-Cortina Clementina R. Mexico�<br />
71 Water Trearment System Using discharge in Water Cavitation�<br />
Department of Electrical and Electronic Engineering, Faculty of Science and Engineering, Saga University�<br />
Satoshi Ihara Japan�<br />
�<br />
105 Effect of ozone-gas bubble size and pH on ozone/UV treatment�<br />
Faculty of Science and Technology, Ryukoku University�<br />
Naoyuki Kishimoto Japan�<br />
117 Decomposition of 1,4-dioxane by ozone and advanced oxidation process�<br />
Sumitomo Precision� Product Shinya Tasaka Japan�<br />
�<br />
Session �10� at Room� ��<br />
�Agriculture-food-beverage application (naitou)�<br />
General presentation�<br />
36 OZONATION OF IMIDACLOPRID AND BITERTANOL: REACTION MONITORING AND EFFECTS<br />
ON CYTOTOXICITY�<br />
Université de Toulouse Bourgin M France�<br />
37 DEGRADATION OF DEOXYNIVALENOL BY OZONATION TREATEMENT:� BY-PRODUCT AND<br />
GENOTOXICITY CHARACTERIZATION�<br />
Université de Toulouse Violleau F. France�<br />
50 Removal of Odorous Compound on Rubber Seals using <strong>Ozone</strong> in Beverage Industries�<br />
Environmental Research and Management Center, Hiroshima University Tetsuji Okuda Japan�<br />
28 <strong>Ozone</strong> Inactivation of food spoilage acid-producing bacteria�<br />
Aichi Gakusen college SIGEZO NAITO Japan�<br />
�<br />
Session �11� at Room� ��<br />
�Industrial Application �Kuzumoto, Nishijima, Lezmik, Liechti��<br />
Page 32
<strong>Ozone</strong> News Volume 37, No.3<br />
General presentation�<br />
80 Application of <strong>Ozone</strong> and Hydrogen Peroxide �O3 + H2O2� AOP �Advanced Oxidation Process� Treatment<br />
to Modify the Surface Characteristics of Single-Walled Carbon Nanotubes �SWNTs� �<br />
R&D Institute of KOLON EFMC Hyung-Nam Lim Korea�<br />
62 Fundamental Studies on Effect of <strong>Ozone</strong> Injection to the Internal Combustion Engine – Chemical changes<br />
of Hydrocarbon Compounds by <strong>Ozone</strong> Injection –�<br />
Sasebo National College of Technology Y. Yagyu Japan�<br />
65 ACID LEACHING OF CHALCOPYRITE WITH OZONE AND FERRIC IONS: TAGUCHI<br />
EXPERIMENT AND STATISCAL ANALYSIS �<br />
Facultad de Metalurgia - Universidad Autónoma de Coahuila�<br />
F. R. Carrillo-Pedroza Mexico�<br />
76 Structural characterization by Nuclear Magnetic Resonance of ozonized triolein�<br />
Department of Ozonized Substances, <strong>Ozone</strong> Research Center, National Center for Scientific Research�<br />
Maritza F. Díaz Cuba�<br />
104 Development of Treatment Technique for Corrosion Inhibitor in Liquid Waste from Nuclear Power Plant<br />
Using <strong>Ozone</strong>�<br />
Toshiba Yuki YAHIRO Japan�<br />
57 Effect and optimization of CO2 partial pressure during ozone water production�<br />
Nomura Micro Science Co.,Ltd. Takahiro Yonehara Japan�<br />
93 Measurement of dissolved ozone concentration with multi-component continuous water analyzer�<br />
Ebara Jitsugyo Co.,Ltd. Yoshio Sato Japan�<br />
133 <strong>Ozone</strong> Measurement Based on optical Absorption Using a Visible LED Source�<br />
The Univ. of Tokushima F. Fukawa Japan�<br />
94 Simple ozone-leak monitor with ultra-violet absorbance system�<br />
Ebara Jitsugyo Co.,Ltd. Nobuyuki Kisaki Japan�<br />
110 Measurement of ozone concentration distribution around small air deodorizer using�<br />
developed ozone detection ribbon�<br />
NTT Energy and Environment System Labs. Yasuko Y. Maruo Japan�<br />
�<br />
�<br />
Session �12� at Room� ��<br />
�<strong>Ozone</strong> Generation �Ito, ��<br />
General presentation�<br />
95 Studies on Discharges Mechanism of Micro-plasma Ozonizer Operated in Water�<br />
University of Miyazaki Tatsuya Sakoda Japan�<br />
103 Fundamental Study of Barrier Discharge and <strong>Ozone</strong> Generation Characteristics for Multiple Needles to<br />
Plane Configuration �<br />
Electrical Engineering and Computer Sciences, University of Hyogo Hideki Ueno Japan�<br />
115 Miniaturized ozone generator for deodorization using ferroelectric LiTaO3 crystal�<br />
Doshisha University Yoshikazu Nakanishi Japan�<br />
116 Reduction of Nox on Air-Fed Ozonizers Using Ferroelectric Packed-bed plasma Reactor�<br />
Department of Electrical and Electronic Engineering, Musashi Institute of Technology�<br />
Yoshiyasu Ehara Japan�<br />
131 Effect dielectric electrode material on ozone generation in piezoelectric transformer-based ozone<br />
generator�<br />
The Univ. of Tokushima K.Teranishi Japan�<br />
132 Consideration on configuration of parallel reactors for ozone production using nanosecond pulsed power<br />
discharge�<br />
The Univ. of Tokushima Fumiaki Fukawa Japan�<br />
Poster presentation�<br />
27 An <strong>Ozone</strong>-zero Phenomena in Pure Oxygen in <strong>Ozone</strong> Generation �<br />
Saga Univ. C.Yamabe Japan<br />
�<br />
�<br />
Session �13� at Room� ��<br />
�<strong>Ozone</strong> Solubilization and Decomposition� �Mizuno��<br />
Key note speech�<br />
143 Absorption and decomposition characteristics of high concentration ozone�<br />
Kyoto University Tadao Mizuno Japan�<br />
Page 33
<strong>Ozone</strong> News Volume 37, No.3<br />
General presentation�<br />
31 Model Development of <strong>Ozone</strong> Decomposition: Validation Using Pure Compounds as Initiator, Promoter<br />
and Inhibitor �<br />
Division of Environmental Science and Engineering, Faculty of Engineering, National University of<br />
Singapore�<br />
E.L. Yong Singapore�<br />
106 Decomposition behavior of dissolved ozone in high temperature solution for decontamination of Reactor<br />
Pressure Vessel in a Nuclear Power Plant �<br />
TOSHIBA Corporation Yumi YAITA Japan�<br />
45 Mass Transfer and Reaction Characteristics of Pressurized Non-Bubble <strong>Ozone</strong> Contactor�<br />
Graduate School of Engineering, Kyoto University Shota Furusawa Japan�<br />
113 Study on ozone absorption characteristics in ultraviolet rays / ozone reactor.�<br />
Kubota Corp. Kodai Yoshizaki�<br />
�<br />
�<br />
Session �Medical� at Room� �<br />
Session Medical 2 Clinical Reports and Treatment Strategies: Angiopathia, Diabetes and Chronic<br />
Inflammatory Diseases<br />
Keynote Lecture<br />
The intensive Care of Lower Limb Diabetic Wounds: our 10 Years Experience in<br />
PatientsTtreated Topically with <strong>Ozone</strong> as Adjunctive Agent.<br />
CALDERON Noam, Teddy Kaufman, Leonid Bryzgalin, Munir Awad<br />
Adjuvant HBO and <strong>Ozone</strong> in Diabetic Foot & Badly Healing Wounds<br />
MAWSOUF M. Nabil 1) , FATHI Ahmed M 2) .,<br />
Session Medical 3 Clinical Reports and Treatment Strategies: Virus Cased Diseases and<br />
Complementary Oncology<br />
Keynote Lecture<br />
<strong>Ozone</strong> Therapy in Cancer Treatment . State of the Art<br />
MENENDEZ Silvia<br />
Practical Session<br />
�<br />
�<br />
Sept. 3 �Thursday� a.m.(9:00-12:05)<br />
�<br />
Session �14� at Room� ��<br />
�Sludge Treatment �Yasui, Liechti��<br />
Key note speech�<br />
4 Power production from municipal sludge using improved anaerobic digestion system�<br />
The university of Kitakyuusyuu Hidenari Yasui Japan�<br />
General presentation�<br />
3 Reduction of sewage sludge and recovery of phosphorus by the ozonation/cavitation method�<br />
Aqua Research Center, The University of Kitakyushu Seiichi Ishikawa Japan�<br />
7 Evaluation of Multistage Anaerobic Digestion Systems combining Ozonation, Mesophilic Digestion and<br />
Thermophilic Digestion�<br />
Dept. of Civil and Environmental Engineering, Tohoku University �<br />
Takuro KOBAYASHI Japan�<br />
98 Ecological Treatment System for River Sludge Sediments using Air & <strong>Ozone</strong> Bubbling�<br />
Institute of Technology, Shimizu Corporation�<br />
Sumio Horiuchi Japan�<br />
99 OZONE POST TREATMENT OF SOLID WASTES�<br />
National Center for Scientific Researcher Matilde López Torres Cuba�<br />
144 Verification of sludge reduction by ozonation with phosphorus recovery conducted at the demonstration<br />
Page 34
<strong>Ozone</strong> News Volume 37, No.3<br />
plant Ebara Corporation Kiyomi Arakawa Japan�<br />
�<br />
129 Performance of sludge disintegration process by ozonation installed in full-scale municipal WWTPs in<br />
Japan�<br />
Research and Technology Development Division Japan Swage Works Agency�<br />
Kentaro Mizuta Japan�<br />
�<br />
Poster presentation�<br />
134 Actinomyces Scum Control-Technology for correcting treatment problems by ozone addition<br />
Kawasaki City Takashi Okochi Japan�<br />
�<br />
�<br />
Session �15� at Room� ��<br />
�Air and Gas Treatment �Sugimitsu��<br />
General presentation�<br />
90 Cooking exhaust deodorization of food processing factory & restaurant with Water Mist &� <strong>Ozone</strong>�<br />
Keihin Sangyo Co. Ltd Noriyoshi Kosaka Japan�<br />
114 Effect of Different Combination of Metal and Zeolite on <strong>Ozone</strong> Assisted Catalysis for VOC Removal�<br />
National Institute of Advanced Industrial Science and Technology �AIST��<br />
Masami Sugasawa Japan�<br />
42 VOC removal in a compact wet scrubber using advanced oxidation process�<br />
Anjou Recherche-Veolia Environnement, Chemin de la Digue;Ecole Nationale Supérieure de Chimie de ��<br />
Rennes;Université européenne de Bretagne�<br />
P.-F. Biard� ��France�<br />
33 Decomposition of Benzene, MTBE and Toluene in Gas Phase by <strong>Ozone</strong>�<br />
Superior School of Chemical Engineering of National Polytechnic Institute�<br />
M. Franco Mexico�<br />
18 Removing Nox Process Having Water Absorption Filter and Effect of <strong>Ozone</strong> Oxidation�<br />
Tada Electric co. LTD Shiro Yamauchi Japan�<br />
107 Catalytic Decomposition of Unwanted <strong>Ozone</strong> under Ambient Conditions�<br />
Carus Corporation Ken Pisarczyk<br />
�<br />
�<br />
Session �16� at Room� ��<br />
�Industrial Wastewater Treatment �Takahashi, Tuyen��<br />
Key note speech�<br />
85 Ozonation of dye stuffs and intermediates and further decrease in dissolved organic carbon�<br />
by post-biogegradation National Institute of AIST Nobuyuki Takahashi Japan�<br />
General presentation�<br />
6 Effect of the Additives on the Degradation of Dyes in Aqueous Solution by Single Ozonation�<br />
Superior School of Chemical Engineering of National Polytechnic Institute �<br />
A. Pérez Mexico�<br />
86 The experimental results of dyeing wastewater treatment by ozonation and biological method�<br />
Institute of Environmental Technology �IET� Vietnamese academy of science and technology �VAST��<br />
Trinh Van Tuyen Vietnam�<br />
47 Dyeing Wastewater Treatment Using Charcoal Made of Vietnamese Bamboo Waste�<br />
ACER, Meisei Univ., Tokyo;Dept. of Environmental Sys., Meisei Univ., Tokyo�<br />
S. Yoshizawa Japan�<br />
74 MELANOIDINS OZONATION FOR COLOR REMOVAL AND ANAEROBIC�<br />
BIODEGRADABILITY ENHANCEMENT�<br />
INRA, UR 50, Laboratoire de Biotechnologie de l�Environnement�<br />
BATTIMELLI Audrey France�<br />
64 CYANIDE REMOVAL FROM AQUEOUS SOLUTIONS BY COMBINED EFFECT OF OZONE AND<br />
ACTIVATED CARBON�<br />
CIEP, Facultad de Ciencias Químicas, Universidad Autónoma de San Luis Potosi�<br />
F. Fraga-Tovar Mexico�<br />
55 OXIDATION OF PETROLEUM REFINERY WASTEWATER CONTAINING PHENOLIC<br />
COMPOUNDS�<br />
Facultad de Química, Universidad Nacional Autónoma de México,�<br />
Page 35
<strong>Ozone</strong> News Volume 37, No.3<br />
Lazcano-Arriola Luz Maria Mexico�<br />
�<br />
Session �Medical � at Room� 4<br />
Session Medical 3 Clinical Reports and Treatment Strategies: Virus Cased Diseases and<br />
Complementary Oncology<br />
Anti-tumor Effect of <strong>Ozone</strong> Water<br />
OKAMOTO Yoshiharu 1) , Takuro Mori 1) , Takeshi Tsuka 1) , Masahiiko Sugiyama 1) , Saburo<br />
Minami 1) , Toru Kitamura 2) , Harunari Okamoto 3)<br />
Intratumoral <strong>Ozone</strong> Therapy - An Important Step in Improving the Control of Tumor Growing<br />
SCHUPPERT, A .<br />
<strong>Ozone</strong> Therapy in Patients with Viral Hepatitis "C”. Ten Years Experience<br />
MAWSOUF M. Nabil 1) and T. Tanbouli 2)<br />
Efficacy of <strong>Ozone</strong> Therapy for Postherpetic Neuralgia (PHN)<br />
TOKUYAMA Hirobumi 1) �Chikaaki Kusaka 2) ,Tsutae NAGATA 2) , Nariko Shinriki 3) ,<br />
Clinical Comparative Study of <strong>Ozone</strong> Therapy and Guideline Therapy in Pressure Ulcer<br />
UEMURA S., T.Ichihara, A.Watanabe, K.Nakahara, T.Yoshimi, J.Uemura<br />
Ozonated Olive Oil Enhances the Growth of Granulation Tissue in a Mouse Model of<br />
Pressure Ulcer<br />
SAKAZAKI Fumitoshi 1) , Hiromi Kataoka 2) , Masanori Senma 2) ,Tomofumi Okuno 1) , Hitoshi<br />
Ueno 1) , Katsuhiko Nakamuro 1)<br />
Components and Anti-inflammatory Action Mechanism of Ozonized Olive Oil<br />
MIURA Toshiaki 1) , Atsushi Iwai 1) , Koichi Tamoto 2) , Akinori Yamazaki 2) , Hiromi Nochi 2)<br />
�<br />
�<br />
�<br />
Sept. 3 �Thursday� p.m.(13:30- 18:30)<br />
�<br />
Session �1� at Room� �<br />
�Water Purification� �Funamizu, Dimitriou, ��<br />
Key note speech�<br />
�� Operating Experience with Drinking Water Ozonation in North America �<br />
Process Application, Inc. Kerwin L. Rakness USA�<br />
General presentation�<br />
34 Evaluation of the raw and process water in the purification plant by Fluorescent Intensity�<br />
Ochanomizu University Nobuyuki Kaiga Japan�<br />
96 Multi-function Sidestream <strong>Ozone</strong> Treatment at a Drinking Water Treatment Plant�<br />
Dessau Inc. Maxime Beaulieu Canada�<br />
92 The reactive art of Quenching Ozonated Water�<br />
Metropolitan Water District of Salt Lake & Sandy Gardner Olson USA�<br />
136 Appropriate ozonation system in water purification plant�<br />
JOA Hirofumi Takahara Japan �<br />
25 Application and operation of high-efficiency ozonation system in combination of pure-oxygen ozonizer�<br />
and U-tube reactor �<br />
Hanshin Water Works Agency Kazuo Ogura Japan�<br />
82 Design of a 2,900 MGD Ozonation System For Taste and Odor Control in Texas�<br />
Black & Veatch Jeff Neemann USA�<br />
91 Application of an advanced water purification�ozonation� system at Murayama Water Purification Plant�<br />
in Tokyo�<br />
Page 36
<strong>Ozone</strong> News Volume 37, No.3<br />
Page 37
<strong>Ozone</strong> News Volume 37, No.3<br />
More scenes from Cambridge Meeting<br />
Page 38
Introducing the Model 465<br />
UV Absorption <strong>Ozone</strong> Analyzers<br />
for all of your gas phase requirements<br />
NIST Traceable <strong>Ozone</strong> Monitors tors<br />
Sample Conditioning Systems ms<br />
Multi-Channel Ambient Monitors nitors<br />
Measuring Ranges from low w ppb up to 400 g/m3 (25% by weight)<br />
Standard Temperature and Pressure Compensation<br />
Exceptional Customer Service<br />
www.teledyne-api.com<br />
9480 Carroll Park Drive, San Diego, CA 92121<br />
20 Years<br />
of Excellence!<br />
For product information<br />
please contact:<br />
2530 Patra Drive<br />
El Sobrante, Ca 94803<br />
Phone: 510-758-5570<br />
Fax: 510-758-5571
OZAT ®<br />
compact ozone<br />
generators<br />
Ozonia is proud to introduce the second generation OZAT ®<br />
CFS-2G ozone generators, incorporating Ozonia’s patented<br />
Advanced Technology non-glass dielectric segments<br />
together with a state-of-the-art IGBT power supply and all<br />
necessary components for safe and continuous operation at<br />
full-load in an industrial environment.<br />
HEADWORKS<br />
BIOLOGY<br />
SEPARATION<br />
MEMBRANE<br />
DISINFECTION<br />
BIOSOLIDS<br />
SYSTEMS<br />
CFS-2G<br />
• Advanced Technology Dielectric<br />
• High ozone concentration<br />
• Compact size<br />
• Robust industrial quality<br />
• Low maintenance<br />
• Simplified controls<br />
OZONIA NORTH AMERICA 491 EDWARD H. ROSS DRIVE, ELMWOOD PARK, NJ 07407 (201) 794-3100 WWW.DEGREMONT-TECHNOLOGIES.COM<br />
ISSN 1065-5905<br />
<strong>International</strong> <strong>Ozone</strong> Association/Editorial Office<br />
P. O. Box 28873<br />
Scottsdale, AZ 85255<br />
Tel: 480-529-3787<br />
Fax: 480-473-9068<br />
Email: info@io3a.org