works approval supporting documentation for … · 1 10-12-2019 final rev1 k barker r t benbow...
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Engineering a Sustainable Future for Our Environment
Head Office: 25-27 Sherwood Street, Northmead NSW 2152 AUSTRALIA
Tel: 61 2 9896 0399 Fax: 61 2 9896 0544
Email: [email protected]
Visit our website: www.benbowenviro.com.au
WORKS APPROVAL
SUPPORTING DOCUMENTATION FOR STERITECH PTY LTD
160 SOUTH GIPPSLAND HWY, DANDENONG
Prepared for: Steritech Pty Ltd
EPA Victoria
Prepared by: Linda Zanotto, Senior Environmental Engineer
R T Benbow, Principal Consultant
Report No: 181187-02_Final Works Approval Supporting Documentation
March 2020
(Released: 10 March 2020)
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COPYRIGHT PERMISSION
The copyright for this report and accompanying notes is held by Benbow Environmental. Where
relevant, the reader shall give acknowledgement of the source in reference to the material
contained therein, and shall not reproduce, modify or supply (by sale or otherwise) any portion of
this report without specific written permission. Any use made of such material without the prior
written permission of Benbow Environmental will constitute an infringement of the rights of
Benbow Environmental which reserves all legal rights and remedies in respect of any such
infringement.
Benbow Environmental reserves all legal rights and remedies in relation to any infringement of its
rights in respect of its confidential information.
Benbow Environmental will permit this document to be copied in its entirety, or part thereof, for
the sole use of the management and staff of Steritech Pty Ltd.
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DOCUMENT CONTROL
Prepared by: Position: Signature: Date:
Linda Zanotto Senior Environmental
Engineer
10 March 2020
Reviewed by: Position: Signature: Date:
Kate Barker Environmental
Scientist
10 March 2020
Approved by: Position: Signature: Date:
R T Benbow Principal Consultant
10 March 2020
DOCUMENT REVISION RECORD
Revision Date Description Checked Approved
1 10-12-2019 Final Rev1 K Barker R T Benbow
DOCUMENT DISTRIBUTION
Revision Issue Date Issued To Issued By
1 10-12-2019 Steritech Pty Ltd Benbow Environmental
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Contents Page
SECTION 1 - GENERAL INFORMATION 3
1. Primary Information 3
1.1 Company Legal Entity 3
1.2 Application Fee 3
2. Land Use 3
2.1 Planning and other approvals 3
2.2 Choice of location for new premises 3
3. Track Record 4
4. Process and Integrated Environmental Assessment 5
4.1 Existing Operation 5
4.2 Description of the Proposal 6
4.3 Process and Technology 8
4.4 Environmental best practice 9
4.5 Choice of Process and Technology 10
4.6 Integrated Environmental Assessment 11
SECTION 2 - ENVIRONMENTAL INFORMATION 12
5. Energy Use and Greenhouse Gas Emissions 12
5.1 General Information 12
6. Water Use 12
6.1 General Information 12
7. Air Emissions 12
7.1 Air Emissions Assessment 12
8. Noise Emissions 13
8.1 General Noise Impact Assessment 13
9. Water 13
10. Land & Groundwater 13
11. Waste 14
11.1 Industrial Waste Generation 14
12. Environmental Management 14
12.1 Risk assessment of non-routine operations 14
12.2 Management System 14
12.3 Construction Impact Management 14
SECTION 3 – OTHER APPROVALS 15
13. Seeking Other EPA Approvals 15
13.1 Commissioning Plan 15
13.2 New Licence or Licence Amendment Subsequent to Works Approvals 15
14. Post Decision – Operational Requirements 15
14.1 Financial assurance 15
14.2 Polychlorinated Biphenyls (PCBs) Management 15
14.3 Monitoring 15
14.4 Reporting annual performance 16
LIMITATIONS 17
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Tables Page
Table 0-1: Nearest Potentially Affected Receptors 6
Table 6-1: General Information (<10 TJ/yr) 12
Table 8-2: Comparison between predicted ground level concentrations (GLCs) of emitted
pollutants and design criteria (Schedule A) of SEPP (AQM) 13
Table 12-3: Estimated future industrial waste generation 14
Table 14-1: Proposed Licence Limits for Air Emissions 15
Table 15-2: Design performance of pollution control equipment 16
Figures Page
Figure 0-1: Location of Subject Site 4
Figure 0-2: Location of nearest sensitive receptors 8
Figure 0-3: Catalytic Abatement Plant Process Diagram provided by Lesni 9
Attachments
Attachment 1: Company Legal Entity
Attachment 2: Site Layout Plan
Attachment 3: Air Quality Impact Assessment
Attachment 4: Environmental Management Plan
Attachment 5: Manufacturer’s Description and Performance Guarantee
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Steritech Pty Ltd
Works Approval Supporting Documentation
Ref: 181187-02_FINAL WORKS APPROVAL SUPPORTING DOCUMENTATION Benbow Environmental
March 2020 Page: 3
SECTION 1 - GENERAL INFORMATION
1. PRIMARY INFORMATION
1.1 Company Legal Entity
The completed company legal entity form is provided as Attachment 1.
1.2 Application Fee
The application fee is the greater of:
1 percent of the estimated cost = 1% x $1,000,000 = $10,000
81.83 fee units (1 fee unit is $14.81 for the 2019-20 financial year) = 81.83 x $14.81 =
$1,212.00
Note: The maximum fee payable is 4,500 fee units ($66,645).
Therefore, the application fee is $10,000 + GST.
2. LAND USE
2.1 Planning and other approvals
A planning permit is required for the installation of the Catalytic Abatement Plant to treat
emissions of ethylene oxide from the existing facility. The planning permit application is being
submitted in conjunction with the works approval application.
2.2 Choice of location for new premises
Steritech already operate the sterilisation facility at the subject site and the land is located at 160
South Gippsland Highway, Dandenong South VIC 3175, and is legally described as Lot 1 TP
921633. The location of the site as shown in Figure 0-1.
The proposed development is for the replacement of existing air pollution control equipment.
Existing flares used for the destruction of ethylene oxide emissions would be replaced by a
catalytic abatement plant. Therefore, key factors for selecting the site do not need to be
provided.
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March 2020 Page: 4
Figure 0-1: Location of Subject Site
Source: Google Maps 2019
Legend: Site boundaries
Benbow Environmental 25-27 Sherwood Street, Northmead NSW 2152
3. TRACK RECORD
In the past three years, Steritech Pty Ltd has received:
No community complaints or concerns;
No enforcement actions from EPA including written warnings, penalty infringements or
prosecutions.
In the past 10 years, Steritech (including directors and persons involved in the management of
the corporation) has not been found guilty of an offence under the Environment Protection Act,
1970, Dangerous Goods Act, 1985, Occupational Health and Safety Act, 2004 or the Equipment
(Public Safety) Act, 1994, nor committed any offence committed outside Victoria.
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March 2020 Page: 5
4. PROCESS AND INTEGRATED ENVIRONMENTAL ASSESSMENT
4.1 Existing Operation
The main site activity is the sterilisation of medical and quarantine products. The sterilisation
process uses ethylene oxide gas to infiltrate the products and packaging in order to kill
micro-organisms by exposing them to the gas under a vacuum in a sealed chamber. Ethylene
oxide (EtO) is an extremely effective sterilising agent for this purpose due to its strong alkylating
properties: it attacks the cellular proteins and nucleic acids of the target micro-organisms,
bringing cell reproduction to a halt and ensuring cell death.
The process of sterilisation with EtO is a three-stage process involving preconditioning,
sterilisation and aeration. In addition to product sterilisation, there is the essential step of air
purification (i.e. control and destruction of EtO before releasing air emissions from the facility).
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March 2020 Page: 6
4.2 Description of the Proposal
Steritech propose to establish new air pollution control equipment for the destruction of
ethylene oxide from their existing sterilisation facility. The existing facility includes two
sterilisation plants, each with its own flare and vertical aeration stack. The new air pollution
control equipment proposed to be installed is a catalytic abatement plant (CAP) that would
replace the flares currently in use for the destruction of ethylene oxide.
The proposal is being pursued on the basis of environmental considerations as a result of an
industrial best practice review of environmental emissions technologies undertaken by Steritech,
with the CAP being found to be the best in terms of destruction efficiency and meeting design
criteria for ethylene oxide. In addition, the flares rely on the consumption of large amounts of
natural gas, which results in higher running costs and a larger carbon footprint compared to
those of the CAP.
Overall, the existing development would not change significantly as a result of the proposal, as
most of the facility’s processes would remain unvaried with the exception of the method of air
pollution control for EtO emissions. Site operations, hours of operation, annual capacity and
employment numbers would remain the same.
Current hours of operation are 24/7. This will not change.
Waste generated by the CAP would include 12,000 Litres of liquid waste from the balancer tank
requiring clean out yearly by a licensed waste contractor. The inactive catalyst (a non-dangerous
good) would require replacing every 5 to 10 years. Waste management is detailed in Section 11.
The nearest sensitive receptors are identified in the table and figure below. The nearest
residential area is 1.59 km to the north-east of the site there are also residential areas 2 km to
the north-west and 2 km to the south-east. The nearest waterway is Eumemmerring Creek, 260
m east of the site.
Table 0-1: Nearest Potentially Affected Receptors
Receptor ID Lot & DP Address Separation
distance Type of receiver
R1 3 PS717564 3/6 Culliver Avenue,
Eumemmerring
1,560 m NE Residential
R2 1 LP23829 2 Olive Road,
Eumemmerring
1,780 m NE Residential
R3 37 LP58583 2 Kays Avenue, Hallam 2,240 m ENE Residential
R4 743 LP201041 4 Affra Place,
Hampton Park
1,930 m ESE Residential
R5 729 LP135000 140 Oaktree Drive,
Hampton Park
2,000 m SE Residential
R6 1 RP14392 1/2 Robjant Street,
Hampton Park
1,960 m SE Residential
R7 9 LP127254 31 Vivien Street,
Dandenong
2,080 m NW Residential
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March 2020 Page: 7
Table 0-1: Nearest Potentially Affected Receptors
Receptor ID Lot & DP Address Separation
distance Type of receiver
R8 20 LP53275 19 Trewin Street,
Dandenong
2,020 m NW Residential
R9 8 LP41759 22 Kirkham Road,
Dandenong
2,000 m NNW Residential
R10 531 LP57859 7 Claredale Road,
Doveton
1,830 m N Residential
R11 7 LP5857 41 Wattle Drive,
Doveton
1,810 m NNE Residential
R12 1 PS437402 22 Power Road,
Doveton
1,840 m NNE Residential
R13 2 PS42760 152-158 South
Gippsland Highway,
Dandenong South
Adjacent N Industrial
Clark’s
Equipment Sales
R14 1 TP174481 170 South Gippsland
Highway, Dandenong
South
Adjacent S Industrial
Tip Top Bakery
R15 1 TP584435 1-9 Hedderwick Road,
Dandenong South
250 m E Industrial
Solos Glass
R16 2 PS443295 95 Greens Road,
Dandenong South
400 m W Industrial
Oceania Glass
R17 1 TP431340 115 S Gippsland Hwy,
Dandenong
380 m NE Commercial
Lunar Drive-In
Movie Theatre
and
Trash &
Treasure Market
R18 2 LP124961 2-4 Round Tower
Road, Dandenong
450 m SE Billiard Halls
R19 1 TP954394 99 Greens Road,
Dandenong South
15 m W Cranbourne Line
proposed raised
rail line
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March 2020 Page: 8
Figure 0-2: Location of nearest sensitive receptors
LEGEND:
Site
Receptor +
Benbow Environmental 25-27 Sherwood Street, Northmead NSW 2152
A site plan is provided as Attachment 2.
4.3 Process and Technology
A Catalytic Abatement Plant (CAP) is proposed to be installed at the Steritech facility in order to
purify exhaust air from the sterilisation and heated aeration chambers. The CAP effectively
converts EtO into carbon dioxide and water vapour, which would be released from a single stack.
The manufacturer of the abatement plant (Lesni) guarantees that the trace concentrations of EtO
in the stack’s exhaust air will meet current European standards (TA-Luft), which demand EtO
emissions of less than 0.5 mg/m3 or less than 0.28 ppm.
The CAP proposed to be installed functions on a two-step system – a balancer tank and catalytic
abator (depicted in Figure 0-3), without the need for using sulphuric acid and without the
generation of glycol waste, unlike other technologies used in the sterilisation industry.
The balancer tank and catalytic abator are designed to operate continuously, for 24 hours a day,
for every day of the year, and can be sized to handle different gas evacuation quantities. The CAP
R19+
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to be installed would be designed to cater for the existing two sterilisation chambers and two
heated aeration rooms used at the Steritech facility.
The system is constructed with an efficient heat exchanger, integrated to recover energy from
the exothermic reaction of the EtO destruction process.
Manufacturer description has been provided as Attachment 5.
Figure 0-3: Catalytic Abatement Plant Process Diagram provided by Lesni
4.4 Environmental best practice
An industrial best practice review of environmental emissions technologies was undertaken by
Steritech in 2015 when considering options for the Sydney facility. The CAP was found to be the
best in terms of destruction efficiency and meeting design criteria for ethylene oxide. Ground
level concentrations of ethylene oxide at nearest receptors using the existing flares and the CAP
have been determined in the AQIA in Attachment 3 to demonstrate potential improvements in
air quality.
Furthermore, the existing flares rely on the consumption of large amounts of natural gas, which
results in higher running costs and a larger carbon footprint compared to those of the CAP.
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4.5 Choice of Process and Technology
In 2015, an Ethylene Oxide Air Controls Study was undertaken for Steritech’s NSW facility. The
purpose of this study was to determine the suitability of alternate ethylene oxide control
technologies for the site with regard to air quality issues. The report presented the following:
Review of world’s best practice control technologies for ethylene oxide in sterilisation
chamber exhaust gas;
Greenhouse gas assessment of proposed air cleaning systems;
Air pollution modelling to predict the ground level ethylene oxide contribution from site
operations with various proposed control systems in place.
A literature review of world’s best practice control technologies found that information on best
practice for the destruction of EtO after the sterilisation process is not readily available, most
likely due to this being a specialised process. The control technologies available and currently
being used at sterilisation facilities around the world, their advantages and disadvantages and
examples were evaluated with the following found to be the preferred method of control for EtO
destruction:
Acid-catalysed scrubber/wet scrubber;
Catalytic converter (catalytic oxidiser and water balance); and
Solid reactant bed filter and wet scrubber.
The total amount of greenhouse gas emissions from a scrubber is approximately 250 tonnes per
annum; from a catalytic converter is approximately 1700 tonnes per year; and the total amount
from a thermal oxidiser is 3000 tonnes per year. The carbon footprint of a scrubber is much less
than that of a thermal oxidiser and is the best choice with respect to reduction in carbon
emissions. A catalytic converter is also significantly better than a thermal oxidiser, reducing the
carbon emissions by over 40%.
Air modelling was undertaken using AERMOD in accordance with the NSW EPA guidelines
“Approved Methods for the Modelling and Assessment of Air Pollutants in New South Wales”,
August 2005 (AMMAAP). The modelling determined the predicted ground level ethylene oxide
contribution from site operations with the various proposed control systems.
The study considered three alternate air cleaning systems; a Bete make scrubber, a Sterimed
scrubber and filter and a Sterimed catalytic converter.
Fifteen (15) scenarios were modelled with systems assumed to be operating under worst case
conditions. Compliance with the Clean Air Regulations and AMMAAP criteria was achieved for all
scenarios with greater efficiency than 99.99%. AMMAAP criteria can be achieved at lower
efficiencies where the stack height is increased.
From this, Steritech originally proposed to switch from the thermal oxidisers to a three stage
scrubber system with a filter. The manufacturer of this system can provide a performance
guarantee of 99.99%. Test data supplied by the system manufacturer demonstrates compliance
with the 99.9999% destruction efficiency criteria and the AMMAAP ground level concentration
criteria but with no guarantee of this performance from the manufacturer in Australia.
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Since then, Steritech reviewed this choice and has obtained approval from Fairfield City Council
and NSW EPA for installation of a Catalytic converter (also called Catalytic Abatement System) at
their Wetherill Park facility for which the manufacturer Lesni can provide a guarantee that EtO
stack emissions will be less than 0.5 mg/m3 (0.28 ppm) which would achieve 99.9999%
destruction efficiency.
4.6 Integrated Environmental Assessment
The impacts on air quality including emissions of ethylene oxide and greenhouse gas emissions
were by far the most significant aspect of the change to pollution control equipment that needed
to be assessed. Noise, waste and water and other environmental aspects were also considered
and assessed to ensure that any potential impacts could be mitigated.
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SECTION 2 - ENVIRONMENTAL INFORMATION
5. ENERGY USE AND GREENHOUSE GAS EMISSIONS
5.1 General Information
The overall level of energy use and energy-related GHG emissions associated with current and
proposed works are provided in the following table. The information provided compares the
existing pollution control equipment with the proposed CAP. All other energy requirements
associated with the operation of the facility will remain the same, the total energy requirements
will be <10TJ/year.
Table 5-1: General Information (<10 TJ/yr)
Works Total annual energy use
TJ/yr
Total energy-related
GHG emissions
tCO2-e/yr
Use of flares (Current) 1.945 TJ 107.8
Use of CAP (Proposed) 1.621 TJ 89.9
There are no non-energy related GHG emissions associated with the proposal.
6. WATER USE
6.1 General Information
The proposed works would result in water usage to remain at <10 ML/yr for the facility.
The current water usage is: 1.8 ML/yr.
7. AIR EMISSIONS
7.1 Air Emissions Assessment
An Air Quality Impact Assessment (AQIA) has been prepared and is provided in Attachment 3.
The following tables below provide a summary.
Model used AERMOD
Met file used A five year (2013-2017) no observation prognostic meteorological data file
was created by Lakes Environmental using the WRF-MMIF model.
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Table 7-2: Comparison between predicted ground level concentrations (GLCs) of emitted
pollutants and design criteria (Schedule A) of SEPP (AQM)
Indicator
Predicted
maximum GLC
(projected)
(mg/m3)
Background
concentration
(mg/m3)1
Predicted
maximum GLCs
(total)
(mg/m3)
Design criteria
(mg/m3)
Ethylene oxide 0.0021 0 0.0021 0.006 1. There are no known EtO generators in the surrounding industrial area to the site. Therefore background
concentrations of EtO can be assumed to be negligible.
8. NOISE EMISSIONS
8.1 General Noise Impact Assessment
The proposed works would not result in an emission of audible noise at the nearest noise
sensitive receptors and there would be no noticeable change in existing emissions from the
facility as it is expected that new pollution control equipment will operate at a similar noise level
to existing equipment. Therefore, a general noise impact assessment has been provided with the
Noise Management Plan which is included as a sub-plan of the site’s Environmental Management
Plan in Attachment 4.
9. WATER
The proposed works would not result in generation of contaminated stormwater.
The premises will not process waste or generate leachate.
The premises will not be scheduled under the Scheduled Premises Regulations as Sewage
Treatment and does not involve operating a wastewater treatment system.
The proposed works does not intend to discharge contaminated stormwater, process wastewater
or treated wastewater to surface water.
10. LAND & GROUNDWATER
The existing and proposed works does not involve any of the following:
Underground storage of petroleum
Pipeline transfer of petroleum
Groundwater extraction
Injection of waste to groundwater
The existing and proposed will not reuse treated wastewater on land.
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11. WASTE
11.1 Industrial Waste Generation
The existing and proposed works would generate less than 1,000 tonnes per year of industrial
wastes.
12.1.1 General Information
A waste management plan is provided as sub-plan 2 in the EMP (Attachment 4). A summary of
waste that would be generated by the CAP is provided in the following table.
Table 11-3: Estimated future industrial waste generation
Type of waste generated Volume Disposal destination
Inactive catalysts material
(From the catalyst chamber in the
proposed CAP. Minimum expected
lifetime of catalyst is 5 years.)
2 T
Once every 5-
10 years
Disposed offsite
Inactive catalyst will be collected in
original receptacle and disposed
offsite to a licensed waste facility
(landfill). The waste is classed as
non-hazardous.
CAP process water – liquid waste
(From the Balancer tank of the CAP.)
Up to 12,000 L
Once yearly
max
Disposed offsite
The process water in the balancer
tank is constantly reused in a closed
loop, but requires replacement once
every year or less. Wastewater will
be collected by a licensed waste
contractor for treatment off site.
12. ENVIRONMENTAL MANAGEMENT
12.1 Risk assessment of non-routine operations
Under upset or non-routine operation conditions there is potential for escape of ethylene oxide
that could cause environmental impacts. A Pollution Incident Response Management Plan
(PIRMP) for the facility has been prepared that explains the risks and precaution measures used
to prevent and minimise environmental impacts. The PIRMP is provided as sub-plan B3 in the
EMP (Attachment 4).
12.2 Management System
The Environmental Management Plan for the facility is provided as Attachment 4.
12.3 Construction Impact Management
The construction activities include installation of the pre-fabricated system on the existing
hardstand area at the site. These activities would not cause significant environmental impacts
such as dust, noise or discharge of contaminated stormwater.
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Steritech Pty Ltd
Works Approval Supporting Documentation
Ref: 181187-02_FINAL WORKS APPROVAL SUPPORTING DOCUMENTATION Benbow Environmental
March 2020 Page: 15
SECTION 3 – OTHER APPROVALS
13. SEEKING OTHER EPA APPROVALS
13.1 Commissioning Plan
Steritech may require commissioning approval under Section 30A of the EP Act and wish to
include the commissioning approval in this application. Steritech understand that upon
completion of works when ready to operated, EPA will be notified and provided with a
commissioning plan that will include:
A timeline
Details of process commissioning (including sequence and test conditions)
Critical control points and the environmental risks
Performance testing (including parameters to be monitored, frequency and reporting).
13.2 New Licence or Licence Amendment Subsequent to Works Approvals
A new licence is required under the Scheduled Premises Regulations. The operations includes air
discharges and proposed limits are detailed below.
Table 13-1: Proposed Licence Limits for Air Emissions
Description of
discharge point
Stack height
(metres)
Emission
indicator
Licence Limit (mg/min) Schedule D or
E of SEPP
(AQM) Existing
(if applicable) Proposed
CAP Stack 10 metres Ethylene
Oxide N/A 83.4 Not listed
The operations will not result in water discharges.
14. POST DECISION – OPERATIONAL REQUIREMENTS
14.1 Financial assurance
The premises is specified under L01 of the Scheduled Premises Regulations and therefore
financial assurance is not required.
14.2 Polychlorinated Biphenyls (PCBs) Management
Not applicable.
14.3 Monitoring
A monitoring program will be prepared for emissions of ethylene oxide as required under the
licence.
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Steritech Pty Ltd
Works Approval Supporting Documentation
Ref: 181187-02_FINAL WORKS APPROVAL SUPPORTING DOCUMENTATION Benbow Environmental
March 2020 Page: 16
14.4 Reporting annual performance
Steritech acknowledge that they will be required to submit an online annual performance
statement with reference to EPA publications 1320 and 1322.
The Pollution equipment manufacturers’ performance guarantees are provided as Attachment 5.
The following table provides the design performance of the proposed pollution control
equipment.
Table 14-2: Design performance of pollution control equipment
Yes Emission indicator Duration
Air emission control equipment X Ethylene oxide 24/7
Noise emission control equipment N/A
Wastewater treatment equipment N/A
Other (please specify): N/A
This concludes the report.
Linda Zanotto
Senior Environmental Engineer
R T Benbow
Principal Consultant
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Steritech Pty Ltd
Works Approval Supporting Documentation
Ref: 181187-02_FINAL WORKS APPROVAL SUPPORTING DOCUMENTATION Benbow Environmental
March 2020 Page: 17
LIMITATIONS
Our services for this project are carried out in accordance with our current professional standards
for site assessment investigations. No guarantees are either expressed or implied.
This report has been prepared solely for the use of Steritech Pty Ltd, as per our agreement for
providing environmental services. Only Steritech Pty Ltd is entitled to rely upon the findings in
the report within the scope of work described in this report. Otherwise, no responsibility is
accepted for the use of any part of the report by another in any other context or for any other
purpose.
Although all due care has been taken in the preparation of this study, no warranty is given, nor
liability accepted (except that otherwise required by law) in relation to any of the information
contained within this document. We accept no responsibility for the accuracy of any data or
information provided to us by Steritech Pty Ltd for the purposes of preparing this report.
Any opinions and judgements expressed herein, which are based on our understanding and
interpretation of current regulatory standards, should not be construed as legal advice.
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ATTACHMENTS
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Attachment 1: Company Legal Entity
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Attachment 2: Site Layout Plan
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Attachment 3: Air Quality Impact Assessment
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Attachment 4: Environmental Management Plan
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Attachment 5: Manufacturer’s Description and Performance Guarantee
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