2.2.1 Initial Installation Visy proposes to initially install a new Paper Machine, Fibre Line and Multi-fuel Power Boiler.. The proposed fuel for the multi-fuel boiler includes paper ma
Trang 1PROJECT SUMMARY and ENVIRONMENTAL ISSUES
For Visy Pulp and Paper, Tumut
Mill Expansion Prepared for NSW Department of Planning
May 2006
Trang 2TABLE OF CONTENTS
1 INTRODUCTION 1
1.1 Background 1
1.2 Increase in Production Capacity 1
1.3 Part 3A EP&A Act 1979 1
1.4 Concept Plan Approval Application 2
2 THE PROPOSED EXPANSION 3
2.1 Overview 3
2.2 Phased Installation 3
2.2.1 Initial Installation 4
2.2.2 Future Installation 5
2.3 Likely Environmental Impacts of the Expansion 8
2.3.1 Air Emissions 10
2.3.2 Odour Management 11
2.3.3 By-products 11
2.3.4 Traffic and Transport 12
2.3.5 Noise 13
2.3.6 Water Management 13
2.3.7 Wastewater Management 13
2.3.8 Socio-Economic Aspects 14
2.3.9 Other 14
2.4 Approvals Required for the Proposed Expansion 14
2.5 Environmental Impacts of Existing Operations 15
2.5.1 Environmental Management 15
2.5.2 Air Quality 15
2.5.3 Odour Management 17
2.5.4 Noise Management 19
2.5.5 By-products 19
2.5.6 Water/Wastewater Management 20
2.5.7 Traffic 21
2.5.8 Community Consultation 22
2.6 Other 23
2.7 Director General’s Requirements 23
Trang 3Visy Tumut – Mill Expansion 1
The current timetable is as follows:
♦ Finalise Environmental Assessments by Q3/2006
1.2 Increase in Production Capacity
Visy Pulp and Paper wishes to increase paper production from its Tumut Plant from the currently approved 300,000 tonnes per annum to 700,000 tonnes per annum
While the existing Development Consent permits an increase of paper production to 450,000 tonnes per annum subject to a further approval in terms of that consent, a new approval is required
to increase paper production to 700,000 tonnes per annum
1.3 Part 3A EP&A Act 1979
The proposed development is a project within the terms of Part 3A of the Environmental Planning and Assessment Act 1979 It comes within Item 4 to Group 1 to Schedule 1 of the State Environmental Planning Policy Major Projects 2005 In this regard, it is a development having a capital investment value of more than $30 million for the purpose of the manufacture of paper pulp and involves paper recycling The estimated cost of the expansion of the plant is a maximum of
$450 million This amount will bring the overall investment in the plant to over $800 million, and see a further 50 jobs created at the mill and a further 350 flow on jobs in supply and service activities
Trang 41.4 Concept Plan Approval Application
For the reasons given below, Visy Pulp and Paper seeks the Minister’s authorisation to lodge an application for a concept plan approval which will give approval to commence specified aspects of the development on receipt of the approval
The concept approval approach is required for Visy Tumut’s future expansion as it is necessary to have up-front certainty for this project as it develops over time The facility itself is a complex one, which also exists within a complex wider framework For example, aspects of Visy’s operations are subject to ongoing changes in critical production technology, some of which are as yet only partly defined The plant is also exposed to changes in the relative availability of recycled paper fibre and virgin fibre, respectively In addition, important factors such as transport, which are external to the facility itself but which have a major bearing on long-term cost competitiveness and regional impacts, need to be taken into account during the project’s medium- to longer-term development
In terms of the facility itself, there are presently a mix of technologies and processing solutions required for the future aspects of the project which may necessitate a number of successive development phases being implemented Hence, some components may be able to be constructed immediately upon receiving approval, whilst others may not be required until later in the facility's overall development For example, the immediate future may require construction of a recycled fibre (RCF) plant, while an anticipated new fibre pulping line component might not be required until supplementary plantation-grown virgin fibre sources become available There are other aspects of the plant that fall within the "immediate" and "later development" classes
Visy’s expansion of its Tumut operation will require significant additional capital expenditure to be raised and committed Visy therefore requires the overall endorsement of the NSW Government, via the planning process, to enable the component parts of this project to proceed with both bankable security and with certainty as to the types of environmental assessments and controls that may be required for components to be developed at a later date than the immediate expansion elements Visy Pulp and Paper is in a good position to assess the likely environmental impacts of the proposed expansion given that it is an expansion of an existing plant which itself was the subject of thorough environmental assessments and was approved subject to a number of conditions
This document is designed to provide:
a An outline of the proposed development (its scale and nature);
b Likely environmental impacts of the proposed development if it is carried out;
c A list of other approvals that are required;
Trang 5Visy Tumut – Mill Expansion 3
Project summary
d An outline of the existing operations of the mill; and
e In doing so, provide information to assist the Department to determine applicable General’s requirements for the project
Director-2 THE PROPOSED EXPANSION
2.1 Overview
Visy Pulp and Paper proposes to expand the existing facility at Tumut NSW by installing a second paper machine and associated pulping capacity This would bring the total approved site production of paper to 700,000 tonnes per year
A number of product options are currently being investigated for proposed mill expansion in order
to address the export market including:
1) A lightweight Kraft Liner Board (as produced by current mill)
2) A lightweight “Kraft Top” sheet, moving to Kraft Liner Board depending on wood supply
availability in the future (mainly recycle sheet with kraft top layer)
3) A white liner
A phased approach is proposed for the mill expansion This will enable some plant components to
be installed immediately, with others being progressively installed over time to meet the project’s expected production milestones Note that it is anticipated to achieve 700,000 tonnes per annum paper production as quickly as possible and required changes will come about from feedstock flexibility A summary of the nature and scope of the proposed development is outlined below
2.2 Phased Installation
Set out below is an indicative description of the expansion phasing and is not intended to be prescriptive The exact phasing of the proposal in terms of the combination of components installed at each phase, and timing of the installation will be subject to the availability of virgin fibre
as well as economic and market forces at the time Therefore, prospects for the “Future Installation” contemplated in 2.2.2 may be brought forward to the “Initial Installation” phase
described in 2.2.1 and subsequently enhanced as supplementary wood fibre becomes available
As such it will be necessary that the approval for the expansion takes into account this need for flexibility
Trang 6The environmental impacts may change between the phases, based on the installed components but the “maximum impact case” will be the benchmark adopted for the purposes of the environmental assessments That is the environmental assessments will be based on the combination of the greatest impacts of each phase, even though the final configuration may not necessarily result in all such impacts
2.2.1 Initial Installation
Visy proposes to initially install a new Paper Machine, Fibre Line and Multi-fuel Power Boiler Production through the existing pulp mill would be increased from 750t/day to 1000t/day This would include modification to the existing Recovery Boiler, Fibre Line, Digester, Lime Kiln, Recasuticising Plant and Evaporation Plant to allow for the increased production The woodyard will be expanded to allow for the increased tonnage of pulpwood, saw mill chips and boiler fuel The mill will continue to operate 24 hours per day, 7 days per week and chipping and debarking operations in the woodyard will continue to run 15 hours per day 7 days per week
Wood and Wastepaper Supply
Depending on availability, the initial installation will utilise approximately 60% virgin fibre and 40% wastepaper This will consist of sawmill residues, softwood pulp logs from State Forests and private plantations, and waste paper from kerbside collections from Sydney and Melbourne In order to produce the white liner product, approximately 30,000 tonne per year of white purchased
pulp will be used
Energy and Steam
Initially a new multi-fuel power boiler is proposed for power and steam generation The proposed fuel for the multi-fuel boiler includes paper machine residues from the existing mill including coarse residues, de-inking and de-ashing sludge De-inking and de-ashing sludge are two streams of residues that are not currently produced by the existing mill and are associated with the use of a higher proportion of wastepaper that is derived from kerbside collection Additionally it is also proposed to utilise paper machine residues from Visy’s existing mills in Sydney and Melbourne as fuel for the multi-fuel boiler The multi-fuel power boiler will be designed to utilise this increased quantity of non standard fuels and will include best available technology for emissions controls There will be an additional stack installed for the emissions from the new multi-fuel power boiler
Water and Wastewater
Fresh water will be supplied via the existing pipeline from Tumut River and stored in the existing fresh water dam onsite The additional quantity of fresh water can be accommodated by the existing pipeline capacity and fresh water dam on site A maximum of 1,600 ML/year of additional
Trang 7Visy Tumut – Mill Expansion 5
Utilities
Natural gas will be utilised as the auxiliary fuel for the new multi-fuel power boiler The additional natural gas requirements can be accommodated by the existing capacity of the natural gas pipeline and metering system on site
A second transformer will be required and, together with associated high voltage equipment; this transformer will be housed in the existing substation on site A connection agreement with Transgrid will be required when activation of the transformer is needed
Stormwater and drainage associated with mill expansion will be connected to the current system since the new components will be within the existing mill footprint The stormwater detention pond may need modification and run off from the expanded woodyard areas may require an additional woodyard first flush dam
2.2.2 Future Installation
When sufficient virgin fibre is available, Visy proposes to shift the fibre mix to approximately 80% virgin fibre and 20% wastepaper and install additional pulp mill capacity This would involve the installation of a new Recovery Boiler, Lime Kiln and Recausticising Plant, Evaporation Plant, and Batch Digester Plant Mill operating hours would continue as per existing operations It is noted that the paper production will remain at 700,000 tonnes per annum
Wood and Wastepaper Supply
As outlined above, this installation will utilise approximately 80% virgin fibre and 20% wastepaper
On site de-inking of wastepaper is proposed as a process mechanism to enable replacement of
purchased white pulp
Energy and Steam
In addition to the multi-fuel power boiler, an additional recovery boiler will be installed The emissions from the new recovery boiler will be directed to the stack servicing the emissions from the multi-fuel power boiler and the new lime kiln A natural gas turbine is proposed to be installed
Trang 8which would result in the mill being 100% self generating with the excess power exported to the grid The emissions from the natural gas turbine will be directed to a separate new stack
Water and Wastewater
The freshwater demand and effluent production will not increase from the initial installation
A list of the additional plant components proposed for the mill expansion is provided in Table 1 over the page A preliminary layout showing existing plant and the proposed expansion components is illustrated in Figure 1
Trang 10Table 1: Mill Expansion – Proposed Plant and Equipment for Phased Installation
Paper Machine–400,000TPY capacity
Fibre Line
80t/hr Multi-fuel Power Boiler fuelled by standard fuel and non standard fuels such
as urban wood residues and paper machine residues from Visy Tumut, Sydney and
Melbourne Mills
Emissions stack servicing emissions from new Multi-fuel Boiler
Log Crane, Stacker Reclaimers, Chipper and fibre storage areas
Recycled Stock Preparation Line
3 additional cooling towers
Transformer, switch gear and cabling
Digester (Batch or Continuous)
750t/day Black Liquor Recovery Boiler
Recausticising Plant and Lime Kiln
Additional Evaporation Line
2 additional cooling towers
Recrystallisation Plant
Wastepaper de-inking plant
40MW Natural Gas Turbine and waste heat boiler
Emissions stack servicing emissions from Natural Gas Turbine
Visy Logistics truck staging facility on Hume Highway to regulate the movements of finished paper and wastepaper to and from the site
Expand/Modify Existing Components
Wastepaper Storage Yard
Wastewater Treatment Plant
Winter Storage Dam and Irrigation Areas
Onsite stormwater drainage
Natural Gas supply arrangement – pipeline and metering station on site for natural gas turbine
NCG Collection System
Condensate Treatment System
1Note that some components of the Future Installation Phase may be brought forward to the Initial Installation Phase subject to wood fibre availability
Trang 11Visy Tumut – Mill Expansion 8
Project summary
2.3 Likely Environmental Impacts of the Expansion
Expansion of the mill will have a number of general environmental impacts associated with it These include:
• Increase in energy and steam requirements for the process therefore an increase in air emissions associated with combustion sources such as boilers and lime kiln
• Increase in noise levels from mill processes due to additional plant and equipment
• Increase in freshwater demand as production is increased
• Increase in fibre resource requirements
• Increase in traffic movements associated with additional fibre resources, boiler fuel, and finished product etc
• Increase in liquid effluent production Associated with this is increasing irrigation infrastructure and irrigation area for the treated effluent
• Increase in the production of solid wastes from the process
Table 2 over the page outlines the maximum key operating parameters for the expanded mill
Trang 12Table 2: Maximum Key Plant Operating Parameters for Expanded Mill
(Maximum input/output)
Wood Demand (incl pulp logs, saw mill residue and purchased pulp)
(Green TPY)
1,950,000
1 Internal Fuel = Bark, fines and Tumut Mill paper machine residue
2 Includes de-inking sludge from proposed future de-inking plant
3 External Fuel = UWR, forest residues, saw mill residues, paper machine residues from Visy Mills in Sydney and
Melbourne
4 Preliminary traffic movements for the mill expansion assumes no back loading and a combination of the maximum
tonnages from the immediate and future installation phases
5 This includes power boiler fly ash and bottom ash, dregs, grits, lime mud, and saltcake Paper Machine residues
from the current Tumut paper machine and the new Tumut paper machine including coarse residues, de-ashing
sludge and de-inking sludge are assumed to be used as fuel for the Multi-fuel Boiler proposed for the mill expansion
The amount of by-products may decrease in the future as virgin fibre sources become more available and less
wastepaper is used which results in reduced production of paper machine residues and therefore less fly ash and
bottom ash is produced
Trang 13Visy Tumut – Mill Expansion 10
Project summary
2.3.1 Air Emissions
There will be additional combustion sources introduced to the site as part of the mill expansion which will result in an increase in the total volume of air emissions to atmosphere The following combustion sources will contribute to the increased emissions volume:
Figure 2: Mill Expansion Combustion Sources
The existing power boiler utilises the mill’s paper machine residues as fuel together with woodyard residues and is permitted to use up to 50% urban wood residues A broader utilisation of non standard fuels is proposed for the multi-fuel power boiler including urban wood residues, paper machine residues from the Visy Tumut paper mills and residues from other Visy paper mills in Sydney and Melbourne Utilising these fuels has the benefit of landfill avoidance of these materials
as well as fossil fuel avoidance thereby minimising fossil fuel based carbon dioxide emissions to atmosphere
Existing Power Boiler
Existing Recovery Boiler
Existing Lime Kiln
Main Stack
Increase flow
by 33%
Initial Installation
New Multi-fuel Power Boiler
Stack
#2
Future Installation
Existing Power Boiler
Existing Recovery Boiler
Existing Lime Kiln
Main Stack
Flow returns to current levels
New Multi-fuel Power Boiler
Stack
#2
New Recovery Boiler
New Lime Kiln
Stack
#3
New Natural Gas Turbine
Existing Power Boiler
Existing Recovery Boiler
Existing Lime Kiln
Main Stack
Increase flow
by 33%
Initial Installation
New Multi-fuel Power Boiler
Stack
#2
Existing Power Boiler
Existing Recovery Boiler
Existing Lime Kiln
Main Stack
Increase flow
by 33%
Initial Installation
New Multi-fuel Power Boiler
Stack
#2
New Multi-fuel Power Boiler
Stack
#2
Future Installation
Existing Power Boiler
Existing Recovery Boiler
Existing Lime Kiln
Main Stack
Flow returns to current levels
New Multi-fuel Power Boiler
Stack
#2
New Recovery Boiler
New Lime Kiln
Stack
#3 New Natural
Gas Turbine
Trang 14The installation of the natural gas turbine will result in the mill being completely energy self sufficient In terms of environmental impact, natural gas is the cleanest of the fossil fuels, particularly compared to coal fired generation in terms of:
• Low Nitrogen Oxides
• Low Particulate Matter without particulate matter control
Process design and pollution control equipment will ensure emissions will be compliant with the NSW Protection of the Environment Operations Act and ambient air quality objectives will be met Holmes Air Sciences has been commissioned to conduct air dispersion modelling in accordance
with DEC (2005) Approved Methods for the Modelling and Assessment of Air Pollution in NSW
2.3.2 Odour Management
Odour management will continue to be a high priority for the expanded operations The NCG collection will be replicated for the expanded plant All odour improvements works that have been made to the existing mill will be incorporated into the design of the new components including the new Multi-fuel Boiler as secondary NCG management to the Recovery Boiler Subject to performance confirmation, the recently installed condensate treatment system will be replicated for expanded operations to minimise odours from sources such as the Paper Machine, Cooling
Towers and Cooling Ponds Odour modelling will be conducted in accordance with DEC (2005) Approved Methods for the Modelling and Assessment of Air Pollution in NSW and DEC (2001) Technical Notes – Draft Policy: Assessment and Management of Odour from Stationary Sources in NSW
2.3.3 By-products
There will be an increase in the quantity of process by-products from the mill expansion including:
• Power Boiler Fly Ash
• Power Boiler Bottom Ash
• Lime Mud
• Grits and Dregs
• Recrystallised Recovery Boiler Fly Ash
• Paper Machine Residues
• Wastewater Plant Sludge
Initially the new paper machine may utilise a larger proportion of wastepaper which is derived from kerbside collections as opposed to box plant clippings which are used by the current paper machine This will produce two types of residue streams, both of which are proposed as fuel for the new multi-fuel boiler The de-inking plant will generate an additional sludge stream which is also proposed as a fuel for the multi-fuel boiler The amount of paper machine residues produced
Trang 15Visy Tumut – Mill Expansion 12
Table 1 in Appendix A shows the maximum expected tonnages of the above by-products from the
mill during the expanded mill operations
2.3.4 Traffic and Transport
There will be an increase in the overall existing traffic movements associated with the mill operations This is associated with the increase in transport of raw materials such as wood fibre, boiler fuel, wastepaper and chemicals as well as an increase in the production of finished product and wastes The use of B-doubles will be maximised and back loading of trucks will be carried out
as much as possible to minimise truck movements The existing routes to and from the mill will be utilised The following table outlines the number of truck movements (two way daily truck movements) predicted in the original EIS for the current operation, actual movements from weighbridge data for current operations, original EIS predictions for the mill expansion and a preliminary estimation of movements from the expanded plant based on the combined maximum of both the initial and future installation phases
Table 3: Two Way Traffic Movements–Original EIS, Current Operations and
Mill Expansion Estimate
Current Operations Mill Expansion EIS Actual
(2005)
EIS Prediction for Mill Expansion 1
Estimated w back loading 2
Estimated w/out back loading 2