EIS 556
AB019265
Mt Gipps Limited : environmental impact statement: proposed
Comet - Hiligrove gold project I
NSW DEPT PRIMARI INAUSTRIES I ABOI 9265 I I I ENVIRONMENTAL IMPACT STATEMENT I PROPOSED ROCKVALE - HILLGROVE GOLD PROJECT I AUGUST, 1989 I I I I I I I I I Prepared by Douglas Martin & Associates Pty Ltd I Environmental Planning Consultants
I in association with
Stuart Miller & Associates Pty Ltd I W.L.P.U. Consultants (Aust) Pty Ltd Nigel Holmes & Associates I Pollution Research Pty Ltd I I ENVIRONMENTAL PLANNING AND ASSESSMENT ACT, 1979 SECTION 77(3)(d) ENVIRONMENTAL IMPACT STATEMENT
This Statement has been prepared on behalf of Mt. Gipps Limited, being the applicant U making the development application referred to below.
The Statement accompanies the development application made in respect to development described as follows:
PROPOSED REOPENING OF COMET GOLD MINE AT ROCKVALE AND TREATMENT OF ORE AND EXTRACTION OF GOLD AT HILLGROVE The development application relates to the land described as follows:
Reference to title
Portion Parish County mi i a ry Volume Folio U Part 154 Clevedon SanV art 4690 20
9856 U Part 163 KfJa.t Part 180 Part 4606 Part 181 " " Part 4607 U Part 184 " Part 4604 Lots 11, 12, 13, Section 21, Brereton Street, Hillgrove and Lot 2, Portion 52, Hillgrove, Metz Parish, Sandon County
The contents of this statement, as required by clause 34 of the Environmental Planning U and Assessment Regulation, 1980, are set forth in the accompanying pages.
Name, Qualifications and Address of DOUGLAS MARTIN & ASSOCIATES PTY LTD person who prepared Environmental ENVIRONMENTAL AND PLANNING Impact Statement: CONSULTANTS 45 Landers Road I LANE COVE 2066
U Certificate U r~~'.R.A.P.I. of DOUGLAS MARTIN & ASSOCIATES PTY LTD U ereby certify that I have prepared the contents of this Statement in accordance with clauses 34 and 35 of the Environmental Planning and Assessment Regulation. U
U :
_ I 1j / 1 MT GIPPS LIMITED
ENVIRONMENTAL IMPACT STATEMENT
PROPOSED COMET/HILLGROVE GOLD PROJECT
AUGUST 1989
NSW DEPARTMENT OF MINERALS AND ENERGY
17 JANO UBRARY
Prepared by:
Douglas Martin & Associates Pty Ltd
Environmental Planning Consultants
In association with
Stuart Miller & Associates Pty Ltd WL.P.U. Consultants Pty Ltd Nigel Holmes & Associates Pollution Research Pty Ltd . ' ; 7 L I E.I.S. I TABLE OF CONTENTS I I IF 1.1 Introduction 1.2 Background I 1.3 Approvals Required 1.4 Project Description I 1.5 Significant Environmental Issues 1.6 Environmental Management Programmes
I 2.0 PROJECT BACKGROUND OBJECTIVES AND APPROVAL PROCESS 2.1 Project Location I 2.2 Project Background 2.3 Project Ownership & Regional Interests 2.4 Project Objectives I 2.5 E.I.S. Objectives 2.6 Environmental Legislation I 2.6.1 Development Consent requirements under Environmental Planning and Assessment Act 1979 2.6.2 Existing Mining Lease I 2.6.3 S.P.C.C. Approvals 2.6.4 Dept of Water Resources Permit I 2.6.5 Public Exhibition
I 3.1 Mining Component 3.1.1 History I 3.1 .2 Tenements & Agreements 3.1.3 Geology I 3.1.4. Ore Reserves 3.1.5 Mining 3.1 .6 Development I 3.1.7 Energy Requirements 3.1.8 Mine Equipment & Installation Requirements I 3.1 .9 Construction 3.1.10 Water Treatment Dam I 3.1.11 Employment I I
3.2 Transport Component I 3.2.1. Traffic Generation 3.2.2 Proposed Transport Route & Alternatives P1 3.2.3 Employment 3.3 Processing Component I 3.3.1 Location 3.3.2 Description of Processing Plant 3.3.3 Construction Schedule I 3.3.4 Employment 3.3.5 Extension of existing tailings facility I 3.3.6 Process Water Recycling System (Decant) I 3.3.7 New Process Water Dam 4.0 EXISTING ENVIRONMENT 4.1 Mining Component I 4.1.1 Climate 4.1.2 Topography I 4.1.3 Soils 4.1.4 Existing Landuse, Tenure & Zoning 4.1.5 Hydrology & Water Quality I 4.1.6 Air Quality 4.1.7 Noise Survey & Existing Background Noise Levels I 4.1.8 Flora & Fauna 4.2 Transport Component I 4.2.1 Topography & Drainage 4.2.2 Land-Use I 4.2.3 Existing Road Network 4.2.4 Road Inventory 4.2.5 Traffic Volumes I 4.2.6 Noise 4.3 Processing Component I 4.3.1 Topography & Drainage 4.3.2 Water Management I 4.3.3 Land Use & Zoning 4.3.4 Noise 4.3.5 Air Quality P1 4.3.6 Socio-economics Li I I 5.0 ENVIRONMENTAL IMPACTS 5.1 Mining Component 5.1.1 Soils 5.1.2 Hydrology & drainage 1 5.1 .3 Land-Use 5.1.4 Traffic Generation I 5.1.5 Noise 5.2 Transport Component I 5.2.1 Evaluation of Alternatives 5.2.2 Traffic Generation 5.2.3 Traffic Safety I 5.2.4 Noise 5.2.5 Dust Generation I 5.2.6 Socio-economics 5.3 Processing Component I 5.3.1 Noise 5.3.2 Air Quality I 5.3.3 Water Quality
~1 1 6.1 Mining Component 6.1.1 Water Treatment Dam I 6.1.2 Noise Managaement 6.2 Transport Component I 6.2.1 Proposed Roadworks 6.2.2 Traffic Management I 6.2.3 Dust Control 6.3 Processing Component 6.3.1 Water Management 1 6.3.2 Existing Water Monitoring Program 6.3.3 Proposed Water Monitoring Program I 6.3.4 Dust Control 7.0 ALTERNATIVES I 7.1 On-Site Processing 7.2 No Action I 8.0 PUBLIC PARTICIPATION 9.0 BIBLIOGRAPHY
I 10.0 STUDY TEAM I APPENDICES 1. Evaluation of Transport Options
I 2. Water Quality Data - Hillgrove I I I I Table 3.1 Comet Mine Resource Statement - May 1988 Table 3.2-1 Proposed Truck Traffic Volumes I Table 3.3-1 Ore Treatment Rates - Hiligrove
I Table 4.1-1 Water Quality Summary - Vicinity of Comet Mine
I Table 4.1-2 Background Noise Levels - Vicinity of Comet Mine
I Table 4.2-1 Study Area Traffic Volumes Origin/Desinat ion Survey, May 1986 and Traffic Counts on MR.74 I Table 4.2-2 Traffic Volumes Roads Maintained by Dumaresq Shire
I Table 4.3-1 Geographic Distribution of Hillgrove Workforce, 1989
I Table 5.1-1 Inventory of Proposed Noise Emission Sources at Comet Mine (No Noise Control Measures in Place) I Table 6.3-1 Parameters for Water Balance - Combined N.E.A.M./Comet Ore I Operation
Table 6.3-2 Proposed Comet/N.E.A.M. Operation - Estimated Water Balance I for Average Annual Climatic Conditions (Year 4)
I Table 6.3-3 Water Quality Monitoring Programme
I Table 7.2-1 Combined Operation Comet/Hillgrove Employment and Income Effects for Each Year of Operation I I I I I I I I 2-1 Location Map I 2-2 Tenement Location & Geology Map I 3-1 Lease, Landholding & Topographic Map 3-2 Geology & Location Map 3-3 Comet Mine Geology I 3-4 Site Plan at Comet Mine 3-5 Conceptual Mine Development I 3-6 Transport Options 3-7 New Processing Plant Location Site Plan I 3-8 Process Plant Flow Chart 3-9 Proposed Water Management Scheme I 3-10 Existing Tailings Facility 3-11 Detail of Proposed Extension of Tailings Facility
I 4-1.1 Evaporation and Rainfall 4-1.2 Temperature I 4-1.3 Wind Data - Armidale 4-1.4 Rainfall Intensity - Rockvale I 4-2 Local Hydrology - Water and Aquatic Fauna Sampling Locations 4-3 Existing Water Management I 4-4 Location and Distribution of Sub-Catchments I 5-1 Location of Houses in Proximity to Transport Route 6-1 Yearly Water Balance - Combined Operation (Year 4) I 6-2 Water Quality Monitoring Locations, Existing and Proposed I I I I I I 'p
I 1.0 SUMMARY
I 1.1 INTRODUCTION
F1 This Environmental Impact Statement (E.I.S.) has been prepared by Douglas Martin & Associates Pty Ltd on behalf of Mt Gipps Limited which is seeking development I consent from Dumaresq Shire Council to operate a processing plant for gold ore at Hillgrove approximately 30km east of Armidale in Northern New South Wales. Gold ore would be transported to the plant from the Comet Gold Mine which is located near I Rockvale and is 42km by road to the north of the proposed Hillgrove plant site. The document has been prepared in accordance with the Director of the Department of I Planning guidelines issued on the 13th March, 1989. This first chapter summarises the planning and other government approvals required, briefly describes the project and goes I on to discuss the most significant environmental issues and outlines any proposed environmental management programmes. I 1.2 BACKGROUND
1 This proposal has resulted from two other proposals to reopen the Comet Gold Mine at Rockvale and carry out processing of the ore immediately adjacent to the mine I (Lewis, 1986; Martin, 1988). The latter of these proposals (Martin, 1988) was given development approval by I Dumaresq Shire Council in January, 1989. For financial reasons, it was then decided to carry out the processing at Hillgrove on a site which is presently used for mining and I processing by the New England Antimony Mine (N.E.A.M.) of which Mt Gipps became a joint-venture partner in May, 1989.
1.3 Approvals Required
I The proposed site is presently zoned rural 1 A under the terms of the Dumaresq Shire Council Planning Scheme. Processing of gold ore is an allowable use of the land I with development consent from the Council. As the processing operation is termed a "designated development" according to the Environmental Planning & Assessment Act, I 1979, an E.I.S. must accompany the development application to Council. I I I 1 2.
i If development consent is granted it is necessary for the proponent (i.e. Mt Gipps Limited) to submit an application to revise its current licences with the State Pollution I Control Commission (S.P.C.C.) for the operation of N.E.A.M.
1.4 Project Description
I Mt Gipps Limited is seeking approval to process 152,000 tonnes over four years of operation at the Hillgrove site. The three main components of the proposal are:
- the mining of the ore from the Comet Mine at Rockvale on an existing mining I lease. - the transport of the ore from Rockvale to Hillgrove along a designated transport I route including Rockvale, Lyndhurst, Tulloch, Chandler, Thorpleigh, Graf ton (M.R. 74) and Stockton (Hillgrove) roads. The maximum number of total truck trips
I would be 24 per day occurring in Year 2 of the operation. In the three other years, the traffic will be significantly less. I - the processing of the ore in a new plant adjacent to the existing antimony I processing plant at Hillgrove using the existing crushing facilities. Mining at Rockvale would be carried out on a two-shift 5 day week basis from I 7a.m. to 11p.m. and transport of ore would occur from the hours 7a.m. to 5 p.m. and only during daylight, Monday to Friday. Processing of the ore would be a three shift 24 I hour operation.
Structures to be built at the Comet Mine include an office and mine facilities building, an access road and a small water treatment dam. There will be some upgrading, realignment and resurfacing on sections of the transport route. The main I construction at the Hillgrove site will be the processing plant, an extension to the existing tailings facility and the construction of an additional dam for storage of I recycle-water. I I I I 1 3. i 1.5 Significant Environmental Issues
The most significant environmental issue raised by this proposal is the transportation of the ore from Rockvale to Hillgrove. This issue was assessed separately I in an evaluation of a number of transport route options (Appendix 1). The preferred route was slightly higher in initial capital cost than another, but it was considered to I have significant environmental advantages. Along the preferred transport route there would be an increase in traffic volume and associated noise level and an increase in dust generation. The other issues relate to the site specific effects of the construction and operation of the plant at Hiligrove. These issues tend to be of lesser significance because of the existing operation of N.E.A.M. which has operated at Hillgrove since I 1969. The proposal will consolidate the operation of Mt Gipps at Hillgrove which presently employs 93 local people and lead to an additional 44 direct jobs within the I region. For the previous proposal (Martin, 188) the residents in the Rockvale vicinity were I concerned about noise generation from the 24 hour operation of the processing plant and the potential for both short and longer term contamination of the downstream water environment resulting from the proposal. For this proposal, the processing plant and the tailings facility will be located at Hillgrove and consequently will eliminate two significant concerns about the previous proposal. I
1.6 Environmental Management
In order to reduce the impact of the trucking operation there have been a number of management programs worked out in conjunction with Dumaresq Shire Council and residents along the route. I These include:
- sealing sections of unsealed roads in proximity to residences and sensitive work I areas (e.g. woolsheds) - improvements to the intersection at junction of Lyndhurst and Tulloch roads I - replacement of a timber bridge on Lyndhurst Road - realignment, widening and repair of drainage to sections of Thorpleigh Road. I - other items listed in Section 6.2 Li] I I 4. I All trucks will be equipped with two-way radios and direct communication between Mt Gipps and the residents along the route would be encouraged with periodic I review meetings to coordinate resident requests for changes to the normal traffic flow. The proponent will also provide back-loading facilities of road building material for I routine or emergency maintenance to any section of the designated transport route. I I I I I L I I I I I I I I I I 5.
I 2.0 PROJECT DESCRIPTION
I 2.1 PROJECT LOCATION
I The Comet Mine is located about 30km north-east of Armidale along the Rockvale Road and a small access road known as Kelly's Road. Hillgrove township, the location of
I the proposed processing plant is approximately 30km due east of Armidale where the New England Antimony Mine (N.E.A.M.) and processing plant has been operating since 1969 (See Fig 2-1). I
2.2 PROJECT BACKGROUND I
This proposal has evolved from a development application in 1988 to reopen the I Comet Mine and process the gold-bearing ore immediately adjacent to the mine at Rockvale (Douglas Martin & Associates Pty Ltd, August 1988). Development consent for
I this previous proposal was given by Dumaresq Shire Council in January, 1989. Following the merger of Mt Gipps Limited with VAM Ltd in April/May 1989 it was decided for financial reasons to process the ore at the existing facilities of N.E.A.M. at Hillgrove I rather than construct completely new facilities at Rockvale. Consequently this project will employ an additional 44 people for the Comet Mine as well as ensure the continued I employment of 93 at Hillgrove which has decreasing in-situ reserves of antimony/gold I ore. 2.3 PROJECT OWNERSHIP & REGIONAL INTERESTS
The combined mining and processing project is jointly owned by Mt Gipps Ltd and VAM Ltd which are both public companies listed on all Australian stock exchanges. Mt I Gipps Ltd has a controlling interest and project management responsibility. In addition to this new investment in the New England region, Mt Gipps is also I developing deposits of an agricultural and industrial mineral in the region near Tamworth. These are the first deposits of the mineral, known as zeolite, to be located I and developed in Australia. I I I I I 2.4 PROJECT OBJECTIVES
I To broaden the mineral base of the Company's present operations.
I To provide an adequate financial base for possible further development of other mines within the Armidale Hillgrove region. I To ensure that the proposed operation is managed in an environmentally I responsible manner. I 2.5 ENVIRONMENTAL IMPACT STATEMENT (E.I.S.) OBJECTIVES 1. To describe the existing environment in the vicinity of each component of the I proposal. 2. To provide comprehensive information on the nature and extent of the U proposed operation. 3. To assess the impact of the proposal. I 4. To propose monitoring and/or management programmes to mitigate any changes to the environment.
I 2.6 ENVIRONMENTAL LEGISLATION
2.6.1 DEVELOPMENT CONSENT REQUIREMENTS UNDER THE ENVIRONMENTAL PLANNING & ASSESSMENT ACT, 1979.
Mt Gipps Ltd retain an existing mining lease on its property at Rockvale. Consent of Dumaresq Shire Council to reopen the mine is required under the requirements of the I Dumaresq Shire Council Planning Scheme. Processing of the ore at Hillgrove requires the construction of a new C.I.P. U (Carbon in Pulp) Plant adjacent to the existing crushing facilities. As more than 100 tonnes per annum of ore will be processed, the new operation is considered to be a I "designated development" under Schedule 3 of the regulations of the Environmental Planning & Assessment Act, 1979. The necessary land for the new processing plant is I presently zoned rural 1 A under the provisions of the Dumaresq Shire Planning Scheme and processing of ore requires development consent from Council. An E.l.S. must be I submitted with a development application to carry out "designated development". I 7. I 2.6.2 EXISTING MINING LEASE
I Mt Gipps currently retain title to Mining Lease (M.L. 755) which covers the area in the vicinity of the Rockvale mine (see Fig. 2-1). Recently maintenance and repair of the I existing facilities has been carried out under the terms of the provisions of the mining lease. I VAM Ltd was the sole operator of the existing antimony mine at Hiligrove until May 1989. This operation has been running since 1969 and currently retains titles to a I number of mineral tenements and applications in the vicinity of the mine. These are shown in Fig. 2-2.
I 2.6.3 S.P.C.C. APPROVALS
An addition to the current pollution control licence from the State Pollution Control Commission (S.P.C.C.) will be required for the new processing plant once I development consent is granted. This revised licence will cover the requirements of the Clean Waters Act (1971), the Clean Air Act (1961) and the Noise Control Act (1975). 1 This licence would be reviewed on an annual basis I 2.6.4 DEPT OF WATER RESOURCES PERMIT There will be a small requirement for domestic water to be pumped from the I Wollomombi River for use in the mine amenities and office area.
1 2.6.5 PUBLIC EXHIBITION I The E.I.S. is to be placed on public exhibition for 30 days and public comment invited. At the end of this period, the E.I.S. and comments received will be used by Council in order to decide whether or not development consent should be granted, 1 granted with specific conditions or refused. Once a decision is made all parties may I appeal to the Land and Environment Court. 1 I I I I 3.0 PROJECT DESCRIPTION
I This chapter describes the proposed project by dividing it into its three major components:
- mining at the Comet Mine, Rockvale I - transportation of the gold ore via Lyndhurst, Tulloch, Chandler & Thorpleigh Roads - processing of the ore at N.E.A.M., Hillgrove. I A balance has been drawn between technical description and the need for communication with interested government agencies, community-based organisat ions I and individuals. However, it should be emphasised that further detail on any aspect of the proposed operation may be readily obtained by direct contact with Mt Gipps Limited I or the authors of this document (see Section 10.0).
I 3.1 MINING COMPONENT I 3.1.1 HISTORY
In the 1870's the Comet mine was known as the Phoenix Gold Mine and was opened I to a depth of about 25m. The North Broken Hill Company Limited investigated it in 1941-42 and concluded from limited diamond drilling that the ore shoots were unlikely Iii to persist to depth. In 1979 the mine was reopened by S.J. Lacey and worked to 1981, over which period a calculated head grade of 8-12 g/t Au was obtained from 8000 tonnes I of ore mined. Since then it has been on care and maintenance. Underground sampling and assessment has subsequently been carried out by Layton I & Associates (1982), Pertzal-Tahan (1983), and United Gold/City Resources (1985) with encouraging results. Mining studies by Murphy (1983) and Magnussen (1985) were similarly encouraging. I City Resources (United Gold/Omega Mining) took up the deposit along with a number of other tenements in the region and drilled it extensively delineating a reserve I of 139,000 tonnes at9.4 g/t Au at a cutoff grade of 3.9 g/t Au. In October, 1987, Mt. Gipps Limited took up an option on the deposit and has I proceeded to a detailed investigation for proposed re-opening. Mt. Gipps Limited now holds an agreement to purchase the property surrounding I I I 9. 1 M.L.755 subject to development consent being granted which is shown in Fig. 3-1. Mt. I Gipps now owns the Happy Valley property which is also shown in Fig. 3-1.
3.1.2 TENEMENTS & AGREEMENTS
Mt. Gipps has purchased City Resource's (Omega Mining) titles to tenements in I the A rmidale region. Those relevant to the Comet Mine are ML 755, covering the mine itself, and I exploration Licence 2728 (Fig. 3-1) which covers areas of potential outside ML 755. An agreement has also been reached with Kratos Pty. Ltd. (Caledon Mining) to I allow mining of ore adjacent to ML 755, within ML(A) 178 (Fig. 3-1). 3.1.3 GEOLOGY
Regionally, gold mineralisation is associated with the contact between I metas ediments and a granitic intrusion (Fig. 3-2). The granite is related to those of the Hillgrove deposits. I The Comet Mine was developed in a quartz reef within the granite, sub-paralleling the metasediment contact. The reef extends over 1500m at the surface and dips southeasterly at approximately 45 degrees into the granite. I Gold occurs in a freemilling quartz lode and is mainly associated with iron sulphides, and with minor lead and arsenic sulphides. I Gold has been deposited by solutions travelling upward through a fault zone. Multiple events have concentrated mineralisat ion within the main lode. A generally I sharp contact exists between the reef and the enclosing host granite. At least one deeper ore shoot has been detected by drilling, which may in fact have provided a conduit for higher deposits. Faulting has also been active since I mineral isation, off-setting the reef. One of the major effects of this has been at the north-eastern end of the ore body where the high grade ore zone has been 'lost' at the I lease boundary. Thus, further drilling may locate additional ore. Surface geology of the proposed site is shown in Fig. 3-3. The mine site plan is shown in Fig. 3-4.
I I I I 10.
3.1.4 ORE RESERVES
The basis for development of the mine is on the proven and probable reserves of 165,563 tonnes of ore at an average grade of 7.3 grams/tonne as outlined in Table 3.1. The actual mineable tonnages however are less than this, due to ore left as support around openings (fig. 3-5). Some additional ore is anticipated from the less defined possible ore zone, yielding a total planned mine production over four years of 151,500 tonnes.
Table 3.1
Comet Mine Resource Statement
May 1988
Geological Insitu @ 4g/t cutoff
CLASSIFICATION GRADE TONNES a/t
PROVEN By Underground Development 10.9 46953 PROBABLE Drill Tested 8.3 118610
- TOTALS 7.3 165563
POSSIBLE Drill Indicated 5.7 46796
- TOTALS 7.7 214000
- POTENTIAL Geologically Inferred 6.0 50000
- Source: Mt. Gipps Limited
3.1.5 MINING
The mine site plan is shown as Fig 3-4. The overall site has a north-east to south-west alignment following the two minor drainage lines which are shown on the figure. The mining area is located around the existing mine shafts which will be used for either mining or venting purposes. These shafts are aligned in parallel to the ore body and run approximately north-east to south-west and are numbered 1 to 5 on the figure. Ore extracted from the mine would be stockpiled and then transported 11.
Li by truck to Hiligrove. The mine has been well developed in the past. There are four shafts which provide I immediate access to the mine. These are Nos. 2, 3, 4 and 5 shafts (see Fig. 3-5). The mine is presently being kept dry and accessible by a pump located on the 3 level at the I bottom of No.2 shaft. No. 2 shaft is well supported with extensive timberwork to the 2 level. The I hoisting arrangements are an air powered winch, a tubular tripod headframe and 0.5 tonne kibbles (bucket) discharging onto a concrete ore pad. The shaft is equipped with a timber skidway to carry and guide the kibble. This shaft has been sunk to the 3 level and I some 15 metres of level development has been done on the 3 level. There is a platform on the 2 level. The portion of shaft between 2 and 3 level has been worked off line and I will have to be straightened. The 3 level has contacted a sheared and faulted zone which will require chemical anchored rockbolts for support. I No. 3 shaft is also well supported with extensive timberwork to the 1 level. The hoisting arrangements are a tubular tripod headframe and a 0.5 tonne kibble discharging onto a concrete ore pad. There is no winch. The shaft is also equipped with a timber skidway to carry and guide the kibble. This shaft has been sunk to the 2 level and has a platform on the 1 level. I No. 4 shaft has been sunk to the 1 level and is bare. No. 5 shaft is also well supported with extensive timberwork to the 1 level. The I hoisting arrangements are a tubular tripod headframe and a 0.5 tonne kibble discharging onto a concrete ore pad. The shaft is also equipped with a timber skidway to carry and I guide the kibble. This shaft has been sunk to the 2 level and has a platform on the 1 level. The 1 level has been driven for 250 metres along the ore-body and I connects Nos. 3 and 5 shafts. It is equipped with 18" gauge rail. Due to the extremely competent nature of the hanging wall it requires minimal support and is accessible for I the entire length along the ore-body. The 2 level has been driven 250 metres along strike and connects Nos. 2, 3 and 5 shafts. It is also equipped with 18" gauge rail. Due to the extremely competent nature of I the hanging wall it similarly requires minimal support and is accessible for the entire length along strike. The northern extremity of the 2 level has contacted a shear zone I with minor faulting and chemical anchored rockbolts will be required to ensure safe conditions for further development and stoping. I I [I I 12.
LI Present equipment on site which is of use include a 500 C.F.M. air compressor Fi which is operational, in good condition but requires sound- proofing. There is also a small workshop, stores and lamproom building which will require upgrading and enlarging.
H 3.1.6 DEVELOPMENT
I The objective is to bring the mine into maximum production as rapidly as possible utilising the existing shaft systems and infrastructure with upgrading as required. The I present hoisting systems are inadequate to handle the relatively higher tonnage rates. The planning and design caters for a maximum production rate of 55,000 tonnes per annum. There would be two shifts of five days a week for the mining operation. I Two distinct mining districts have been identified. Poor core recovery from diamond drilling in particular recovery of the granular sulphides and the relative I inaccuracy of percussion and reverse circulation drilling leave open the question of continuity of economic grade at depth. Continuity of the mineral ised body at depth is I confirmed in terms of reef thickness which increases with depth. No. 5 shaft will be re-equipped with a steel headframe and 80 H.P. hoist and will I provide immediate access for men, materials and machinery to the 1 and 2 levels for the rapid rehabilitation of the drives and stopes on those levels. No. 2 shaft will be used as a sinking, development, raising, materials handling and I man-hauling shaft. It will be sunk another 30 metres based on present drilling information. It will be equipped with a single 3-tonne capacity skip with provision to 1 lower and raise men, materials and machinery. It will also be equipped with a ladderway and will accommodate compressed air and water piping. It will be necessary to remove Fill the present headframe, hoist and hoisting gear to make way for a new higher capacity hoisting system. F~ Access to the ore-body will be carried out by driving along the lode. Extension of 1 and 2 levels southward towards the lease boundary and delineating ore blocks for later extract ion. No. 3 shaft will be used for temporary access during rehabilitation and I re-equipment and then become an upcast ventilation shaft.
IL~ I I I I 13. I 3.1.7 ENERGY REQUIREMENTS
I There is a 200 KVA 415 V power supply on site. This facility will be upgraded to 300 KVA by installation of a new transformer. Total power requirements for the project I will be 280KVA.
I 3.1.8 MINE EQUIPMENT & INSTALLATION REQUIREMENTS SURFACE FACILITIES I AMENITIES BLOCK 6 Showers 2 Toilets 1 Urinal I 25 Lockers - wet - dry
I LAMP ROOM
LAMPS I Charging racks: 35 cap lamp capacity I EXPLOSIVES STORAGE Gelignite: A magazine suitable for storage of 100 (size 25kg) cartons. For location I see Fig. 3-4. Electric detonators: magazine suitable for storage of 2000 detonators. ANFO Preparation:.. storage shed for approximately 10 tonnes of nitropril in 40 kg 1 bags small motorised ANFO mixing machine I ANFO silo HOISTING I No.2 shaft -80 Kw AC hydraulic winch, headframe, tipple, bin, winch shed and 1.5m3 capacity skip. I -- No. 5 shaft - 80 Kw electric hydraulic double drum winch, headframe, tipple, bin, winch shed and 1 .5m3 capacity skips in I balance.
1 PRIMARY VENTILATION
I Nos. 3 & 4 shafts: Centrifugal fans, 40kW motor, 50,000 cfm. I I 1 14.
COMPRESSED AIR
-- 1 x diesel compressor, 600 cfm at 100 psi. -- 3 x Electric Compressors, each 550 cfm at 100 psi. -- 1 x Air Receiver. -- Distribution main. -- Weather proofing and sound attenuation housing.
WATER SUPPLY (DRILLING AND ABLUTIONS) -- 2 x 22,500 litre (5000 gallon) storage tanks. -- Mine reticulation system with pressure breakdown using reducing valves.
111,V11,1121
- Timber handling and storage area. -- Shed to house docking saw, chainsaws etc. STORES
-- Shed to house general stores items. -- Storage area for rails, pipes, mesh, roof bolts.
UNDERGROUND FACILITIES DRILLING EQUIPMENT
Drilling machines (Atlas Copco Panther BBD91 or equivalent) Air legs - single stage (Atlas Copco BMK91 R) - double stage (Atlas Copco BMK51T6R) or equivalent air legs
Drill Steel Grinders Air line oilers (automatic low oil shut off) Air line oilers - ordinary type 15.
BLASTING EQUIPMENT
Portable ANFO Loaders Electric Shot Firers (I.C.l.) Firing Circuit Testers
RAIL EQUIPMENT - 61 0mm (24-inch gauge)
Air shovels either Eimco 12B or Atlas Copco LM36 plus major spare components - traction motor -. bucket motor Battery Electric Locomotives (Gemco 1.5 tonne) Trucks (1 tonne capacity, side tipping)
SECONDARY VENTILATION
-- 3 x 2 stage axial flow electric fans 7.5 kW each -- 2 Centrifugal fans -- 3 x 150mm diameter venturi ventilators -- 3 air fans (350mm-450mm diameter)
PUMPS
-- 4 submersible centrifugal pumps, compressed air operated -- 2 diaphragm pumps, compressed air operated (Atlas Copco DOP15) -- Mine drainage pumps - 1 electrically operated pump 1 spare pump
WINCHES (Compressed air operated)
-- Shaft sinking (2 x 1 tonne capacity winches) -- Stope materials handling (5 small winches)
SCRAPER
-- 2 small compressed air operated scraper winches and hoes 16.
SAWS
-- 5 compressed air operated chain saws
HAND DRILLS
-- 2 x 12m electric drills -- 2 x 12m air operated drills -- 3 x lOm air operated pistol drills
3.1.9 CONSTRUCTION
Construction of the mine facilities will commence once development consent has been granted. As much of this work will be carried out underground, surface activity will be limited to:
- the construction of an earth dam of capacity 0.4 Megalitres which will be used to treat water pumped from the mine
- reinforcement of No. 2 shaft collar
- the construction of an amenities block and office facilities
- a pad for two winder sheds
- road and drainage construction.
These surface activities will continue for up to three months with the majority of the on-site work being completed within 8 weeks. The proposed road and other surface activities are shown in Fig. 3-4. Construction would only be carried out in daylight hours from 7.30a.m. to 4.00p.m.
3.1.10 WATER TREATMENT DAM
The proposed location of the dam for treatment of the mine-water is shown in Fig. 3-4. The surface area of this dam will be approximately 20m x 20m in surface area and will be used to ensure that no contaminated water is allowed to flow into the drainage line adjacent to the mine. I 17. 3.1.11 EMPLOYMENT
I The mine will run on a two-shift basis from 7a.m. to 3p.m. and 3-11p.m. Total I employment at the mine will be 39 people. I 3.2 TRANSPORT COMPONENT 3.2.1 TRAFFIC GENERATION I The project has a projected life of four years and the required tonnages for each year are as shown in Table 3.2-1. I As can be seen in the table, the maximum movement is required in Year 2 of the operation when the annual tonnage reaches 55,000 tonnes. Assuming a 236 day/year, the I maximum number of daily trips was calculated at 24. Operations would be carried out for five days a week from 7a.m. to 5p.m. using trucks of 20-22 tonne capacity. If the I number of working days/year were to increase the number of truck movements necessary per day would decrease to maintain production. E There is adequate storage area adjacent to the Hillgrove processing plant for stockpiles of up to 21 days of material.
I 3.2.2 PROPOSED TRANSPORT ROUTE & ALTERNATIVES
A number of options were considered for the transport of the Rockvale (Comet) ore. These are shown in Fig. 3-6. The preferred route chosen from the evaluation of options was Option 3 which involves sections of Rockvale Road, Lyndhurst Road, Tulloch Road, Chandler Road, Thorpleigh Road, Graf ton and Stockton (Hillgrove) Road. The overall journey length is 42km of which 16km is sealed and 26km is unsealed.
3.2.3 EMPLOYMENT
In order to satisfy project requirements up to 5 contract jobs would be created for drivers and maintenance. Two trucks would be required in years 1, 3 and 4 of operation I with three trucks required in year 2 of the operation. I I I
18.
TABLE 3.2-1
PROPOSED TRUCK TRAFFIC VOLUMES
Year 1 Year 2 Year 3 Year 4
Tonnes Hauled 24500 55000 40000 32000
Total Annual Loads 1255 2750 2000 1600
Total Trips 2450 5500 4000 3200
Daily Trips 236 Day Year 10 24 18 14
Hourly Volume 7a.m. - 5p.m. 1 2.4 1.8 1.4 Source: Mt Gipps Limited
3.3 PROCESSING COMPONENT
3.3.1 LOCATION
The new processing plant f or the Comet ore would be located immediately to the south-west of the existing antimony processing plant (see Fig.3-7).
3.3.2 DESCRIPTION OF PROCESSING PLANT
SUMMARY
The plant will be integrated into the existing operation of N.E.A.M. The basic production process of the C.I.P./C.I.L. plant is shown in Fig. 3-8. It should be emphasised that the proposed plant will be a scaled down version of the design put forward in the previous E.I.S. for on-site processing at Rockvale.
The process will:
use the existing Crushing Plant require building new Grinding, Cyanidation, adsorption and gold production areas. I 19. The existing crushing plant used by N.E.A.M. would also be used for crushing of I the Comet ore.This plant would be run in cycles of approximately 6 days predominantly during day shift.
I The grinding, cyanidation and adsorption section is designed as a continuous (24 I hour/day) operation. The other area is the gold room consisting of the elution, electro- winning and I gold smelting section. This section will be a 5 day/week, day shift operation. I CRUSHING & SCREENING
There is an existing two stage crushing plant. It consists of a double toggle jaw I crusher 610 x 91 0mm and a 1200mm gyratory crusher operating in closed circuit with a 1 .22m x 3.05m double deck screen. The plant will treat ore at an average rate of 40 I tonnes/hour and produce a product of nominally minus 11mm. The ore will be fed to the primary crusher va an apron feeder which will remove I -80mm fines from the Run of Mine (ROM) feed. The primary jaw crusher product/screen feed conveyor is 750mm wide and the I return oversize conveyors and final product conveyors are 800mm wide. The final crushed product will pass to a fine ore bin of 500 tonnes live capacity equivalent to 8 milling shifts. I Dust suppression is fitted at the discharge of the secondary crusher. Maintenance of the existing crushing plant equipment is by hoist and no provision I has been made in the plant design for lifting hoists. Tramp metal detection has been provided by the inclusion of a magnet and metal I detector on the screen feed conveyor. A small control cab houses all the electrical starting equipment and provides shelter for the operator. I Ahead of the primary crusher there is an area of about 30m x 50m for ROM ore storage of about 5,000 tonnes.
I I I 20.
GRINDING
I The mill and cyclone have been sized to treat 6.5 tonnes per hour of feed and produce a cyclone overflow product of 80% minus 75 microns at a pulp density of 40% I solids. A vibrating screen 3.05m x 1 .22m screens the cyclone overflow to remove tramp I oversize and wood fibre. pH control is obtained by adding metered amounts of lime via a variable speed I rotary feeder to the mill feed conveyor. I LEACHING & CARBON ADSORPTION I The majorsteps in this section are:-
Step 1 - Aeration
I Ground pulp at 40% solids will gravitate from the grinding circuit cyclones via the trash removal screen to two pre-leach tanks in series. Each tank, of 45 m3 live volume would be fitted with dual open impellers. Residence time in I the tanks will be 2.5 hours per tank.
Both tanks will be strongly aerated to ensure adequate leach rates in the following leach tanks.
Step 2 - Leaching
Leaching would be carried out after preliminary aeration to control cyanide consumption and to raise the dissolved oxygen to a level acceptable for I leaching. Aeration will continue in all leach tanks.
Two tanks of similar configuration to the aeration tanks would be provided for this task. I Cyanide solution normally will be metered to the first leach tank with I facilities to feed to the second tank should the first be out of commission. I I 21.
i Step 3 - Carbon Adsorption
I Five tanks, operating in series and fitted with dual open impellers, will operate as a carbon-in-leach train. Each tank, 3700mm diameter x 4000mm high provides 3.5 hours retention time.
Each tank would be fitted with Kambalda type interstage screens.
Carbon transfer from tank to tank would be counter-current to the pulp flow I and would be achieved by internal air lifts. The final stage of carbon transference is by means of a submersible vertical recessed impeller pump I which delivers loaded carbon, via a screen to remove surplus pulp, to the I elution column, the surplus pulp returning to the first CIL tank. Pulp discharge from the final tank in the train would be screened on a I horizontal vibrating screen, to minimise carbon loss, prior to pumping to the tailings dam.
I The plant has been designed for a carbon concentration in the range of 20g/I with an average carbon inventory per tank of 860kg. Total carbon advance can I be achieved within an eight hour shift.
I ELUTION
I The complete elution procedure is carried out on one bed volume of carbon 0 cub.m equivalent to 500kg carbon) in a butyl rubber-lined column of 600mm inside diameter x 3600mm height. I
The elution procedure can be controlled in either automatic or manual mode I with interlocks and controls for the circuit.
The elution procedure consists of the following stages:
I - Acid wash - Water wash - Pretreatment with a caustic/cyanide solution I - Water elution - Cooling I I I Step 1 - Acid Wash
I The acid wash is carried out at ambient temperature for 20 minutes using 0.67 I Bed Volume (BV) of 3% strength acid. Step 2 - Water Wash
The purpose of the water wash is to remove residual hydrochloric acid from I the carbon before treatment with caustic and cyanide. The wash is carried out at 90 degrees C for 120 minutes using 4 BVs of water. I Step 3 - Pretreatment
A premixed caustic and cyanide solution is pumped into the column at 2 BVs I per hour using a positive displacement pump. A solution temperature of 110 degrees C is achieved by: I a. reclaim of heat from column exit solutions in a heat exchanger; and b. heat transfer from the boiler section which is separately circulated I through the heat exchanger.
The pretreatment is done for 20 minutes and all solutions are collected in the 7 m3 capacity electrolyte tank, ready for electrowinning.
Step 4 - Elut ion I The elution cycle is carried out at 110 degrees C using the heating method described above. This phase of the cycle (6 BVs) utilises potable water and the I subsequent eluate passes to the electrolyte tank for electrow inning. I I I I I I 23. i Step5-Cooling
I This final step is necessary to prevent boiling of water in the column when I removing the carbon and to stop any further elution of gold from carbon. The cooling water is discharged to the electrolyte tank.
Step 6 - Barren Carbon Transfer I Barren carbon is hydraulically discharged from the column to the regeneration kiln feed vessel. It is also possible to discharge the carbon directly into the I last stage of CIL, thus bypassing the regeneration stage. Transfer is affected in about 60 minutes using 2 BVs of
I raw potable water. I Ultimate transfer of carbon, after regeneration, back to CIL is by a dense I - phase conveying technique using process water. This minimises carbon I attrition.
I The purpose of regeneration is to reactivate carbon and also to remove organic compounds such as oils that adsorb on to the carbon during pulp and
I carbon contacting. The reactivation is necessary as loss of activity of the I carbon can result in loss of gold from the plant in solution form. I Eluted carbon is transferred to the kiln feed vessel and the water allowed to drain. The vertical kiln is heated by gas burners to a temperature of 650 degrees C. The drained carbon is fed by a screw feeder at a rate up to 50 kg/h I into the kiln, where the carbon is regenerated at 650 degrees C for 15 minutes. I I I 24. I The regenerated carbon is transferred hydraulically from the transfer vessel I to the last CIL tank. I GOLD RECOVERY I Electrow inning is used to remove gold from the electrolyte solution. The gold I is deposited on to steel wool cathodes.
The loaded gold solution from the elution column is circulated through a I rectangular electrow inning cell of 9 cathode capacity 0.5 m3/h. Electrow inning is carried out for up to 16 hours per day or until low I electrolyte gold levels of about 3g Au/t are attained.
I Each cathode consists of about 0.4kg of steelwool and gold loadings of about 2kg per cathode can be expected after two campaigns. Barren electrolyte is I pumped to the first preleach tank.
The loaded cathodes are removed from the cells about 3 times per week. The I cathodes are smelted to remove the steel wool and gold is poured into standard moulds and cooled. Slag is returned to the mill to recover residual I gold.
I The proposed layout of the plant has been integrated with the grinding circuit in order to minimise space wastage and provide easy access around the main I areas of the plant.
The ground floor is suitably sloped for spillage drainage into floor sump I pumps, one serving each of the grinding and leach sections, and the tailings I pumps. The floor of the gold room has been divided into separate bunded self draining I areas for acid, caustic cyanide and the main area of the gold room. Any spills in the acid or caustic cyanide areas will empty by means of a small hand I pump. The main floor area of the gold room will be serviced by a vertical sump pump which will transfer any spillage, washings to the CIL section of H the plant. I 25. I I GENERAL
I All bulk reagent storage would be held in a separate locked fenced of f area adjacent to the reagent mixing section alongside the CIL section of the plant. I This area would be bunded and drain to a holding tank for transfer to the tailings storage area. Fj' A safety shower with eyewash will be provided to service this area.
A separate gas storage area has also been provided to service water heaters, LI kiln and bullion furnace within the gold room. LIME ADDITION I Lime would be delivered to site as quicklime in 20 tonne bulk tankers which I would be pneumatically discharged into a 40 tonne capacity silo. The lime would be metered from the silo directly on to the mill feed conveyor where it I would be ploughed into the ore to prevent dusting. I CYANIDE The cyanide mixing system, sited adjacent to the CIL section, is designed to I accept bulker bags of sodium cyanide. The bags are hoisted on to a dry bag breaker fitted with a cruciform knife discharging into a mechanically agitated I above-ground mixing tank. To prevent volatilisation of HCN from the cyanide solution an alkali pH would be maintained using a small amount of caustic solution. The cyanide solution is transferred by pumping to an above ground I storage tank which has about 24 hr storage capacity. Cyanide addition to the I leach circuit is by a variable speed positive displacement pump. The mixing area is fully bunded and floor slope drains to the floor pump I servicing the CIL section of the plant. Cyanide solution would also be pumped as required from the storage tank to the caustic I LI I I 26. I cyanide solution tank provided for the elution circuit. I The small requirements for caustic cyanide solution and acid required for the elution and gold room sections will be mixed as required in separate 2 m3 I tanks and the solutions will be added to the elution circuit by variable speed positive displacement pumps.
Safety control measures for occupational health and safety include:
- The plant to be fully serviced with washing and shower facilities in the cyanide mixing areas, liquor storage tank areas, addition points, grinding I and adsorption circuits, and in the carbon stripping areas.
- Regular inspection of water pumping facilities to ensure maintenance of water pressure for washing and shower facilities.
- Provision of oxygen and air resuscitation equipment.
- Education of plant staff on recommended first aid procedures for cyanide use. I
- Provision of personal hydrogen cyanide detectors and cyanide antidote I kits.
I - Liaison with local fire and hospital facilities. Transport of sodium cyanide to the site would continue to be carried out in accordance with 1 the requirements of the N.S.W. Dangerous Goods Act. One 20 tonne load of sodium cyanide would be required per month of operation. It should be noted that sodium cyanide is already used in I the antimony plant for batch treatment of gold concentrate to bullion. I I I I I 27. I 3.3.3 CONSTRUCTION SCHEDULE
I The construction of the processing plant should take approximately 6 months to complete and involve a peak workforce of 20-30 workers. Total capital investment I involved in the project is approximately $M2.0. The workforce would be accommodated in Armidale. I The process plant construction would require the delivery of major pieces of equipment such as the ball mill. It would also require the delivery of fabricated steel I and construction materials. Construction would only be carried out during the daytime from 7.30a.m.-4.00p.m.
3.3.4 EMPLOYMENT
I The processing plant will require a workforce of 6 who would operate the plant I over three shifts per day. 3.3.5 EXTENSION OF EXISTING TAILINGS FACILITY I PROJECT REQUIREMENTS
I The existing operation at N.E.A.M. involves the production of approximately 40,000 tpa of tailings which are deposited in the existing tailings dam. Introduction of I the Comet Valley ore and associated increase in N.E.A.M. production for a four year period requires an addition to the tailings facility to accommodate approximately an I extra 326,000 tonnes of tailings produced at a rate of approximately 90,000 tpa. It is planned to treat N.E.A.M. ore and Comet Valley ore concurrently and the planned rates I of production are shown in Table 3.3-1. The lay-out of the proposed extended operation is shown in Fig. 3-9.
I TABLE 3.3-1 I Proposed Ore treatment rates - Hillgrove Rate (tpa)
I Ore Year 1 Year 2 Year 3 Year 4
N.E.A.M. Ore 46,500 35,000 46,500 46,500 I Comet Valley Ore 24,500 55,000 40,000 32,000 I Source: Mt Gipps Limited I
I DESCRIPTION OF PROPOSED EXTENSION
I The tailings storage facility at N.E.A.M. was constructed in 1983 upon the commencement of a tailings retreatment programme, which reclaimed all of the I previous tailings storage areas. The impoundment is built in a deep valley, and is basically of upstream I construction. The tailings facility is designed to a maximum height of 37m and with an overall slope of 3 (horizontal) to 1 (vertical). The face of the main embankment is constructed in a series of five steps, three lOm high and separated by 12m wide benches followed by a five metre high step, 6m wide bench and three metre high step to the top of the embankment. A cross section of the existing facility is shown on Figure 3-10. I For the first two years of its life, tailings were cycloned in the plant to provide
two separate tails streams - a coarse fraction, which was placed upstream of a rockf ill I starter toe wall, and a slimes fraction which was placed in a separate containment in a position near the centre of the ultimate storage area. Each successive major lift of the
~7' embankment was constructed using locally excavated rockf ill placed by the upstream method in approximately 2m high lifts and cycloned coarse fraction tailings placed I behind each lift forming the foundation for the next small rockf ill embankment. Extensive underdrainage, comprising agricultural drains covered with graded filter material was placed along the valley floor, fanning out to drain the entire toe area of I the valley dam. These drains flow to a separate catchment dam downstream, where water is recycled to the main Eleanora Dam along with decant water. I Additional storage required for the 326,000 tonne of tailings will be provided by a 6m high paddock type storage constructed by the upstream method in two 3m lifts on I top of the existing facility. The new storage will be 160m x 300m and extend into the abutment on the northern side of the existing storage. The embankments will be I constructed from rockf ill obtained from this northern abutment. Current deposition procedures whereby tailings are beached from the embankments provide a foundation onto which a staged 6m high embankment may be I placed. Past construction has demonstrated the viability of this approach and stability analysis, using conservative parameters, has demonstrated acceptable factors of safety. I Further stability analyses using the models analysed for the present situation demonstrate that the proposed addition does not impair the existing factors of safety.
I I I Deposition will take place from the perimeter of the storage and the final freeboard at the perimeter will be 0.5m. Additional flood storage will be gained from in the storage formed by the sloping beaches from all sides to the existing central drain. Total final flood storage at the end of the life of the operation will be 40,000m3 or equivalent to the runoff from 830mm of rainfall i.e. 3.6 times the rainfall from a 1/100 yr 72 hour storm.
SUBAERIAL DEPOSITION
Tailings will be pumped to the tailings storage in slurry form at 23% solids for the N.E.A.M. tailings and at 40% solids for the Comet tailings and then deposited around the perimeter of the tailings storage according to a predetermined strategy based on the subaerial deposition technique. This technique has proved most suitable for Australian conditions. The location of the proposed perimeter tailings distribution line and a cross section of the proposal is shown on Figure 3-11. Experience has shown that deposition in thin layers, when dried by evaporation, results in the establishment of a competent tailings mass which is not subject to further settlement or consolidation, and is stable even under severe loading conditions. The perimeter distribution pipe will be laid on the crest of the embankment on all four sides and a number of smaller diameter off takes spaced evenly along the length of the distribution line. The flow of tailings slurry from each off take will be directed into the storage through a pipe to the surface of the stored tailings in order to prevent erosion and to allow non turbulent deposition of the slurry, hence efficient settling and supernatant production. The entire surface of the tailings storage will be covered with a generally even layer of tailings and the selection of off takes will be controlled to ensure an even distribution. Within the storage the tailings will be discharged on a cyclic basis, each deposited layer being permitted to settle, dry and consolidate prior to the placement of the next layer. The deposition strategy will produce a gently dished surface sloping towards the central decant riser. I 30. i 3.3.6 PROCESS WATER RECYCLING SYSTEM (DECANT) I Water balance calculations (Section 6.3) show that under average climatic conditions, peak flows required at the decant will increase by about 50% to 5.2 I/s. This I capacity can be accommodated by the existing decant system. However, in order to allow separation of cyanide contaminated water from the I existing N.E.A.M. tailings an additional decant system is proposed. This system will allow sub-division of the drainage from the tailings and will comprise a tower structure I located against the northern edge of the facility and founded on natural ground. This tower will be able to gravity feed return water directly back to the plant or water I storage.
3.3.7 NEW PROCESS WATER DAM I
DESCRIPTION OF OPERATION
Operation of the Comet/N.E.A.M. project will involve a water management plan I which is designed to isolate all cyanide process water and reserve it solely for recycle to the process plant. Make-up requirements will be met from Eleanora Dam. To achieve this a new process water dam is proposed and is sited to the north of Eleanora Dam. The I dam will be a four sided impoundment with rainfall runoff only being received from incident rainfall. It will be 75m square, contain water to a maximum depth of 2.7m and I have a capacity of 15 Ml. During periods of extreme rainfall or reduced recycle any requirement to spill process water from the new process water dam will be I accommodated by a spillway leading into the Eleanora Dam (see Figure 3-9). Water from the tailings dam and underdrainage from the seepage dam will be I pumped directly to the new process water dam for direct recycle to the plant as required. Make-up water will be pumped from the Eleanora Dam. The existing water return dam will be removed from the system. I Uncontaminated rainfall runoff will bypass the Eleanora Dam via the existing overflow bypass channel and be diverted around the diversion pipes immediately I downstream of the Eleanora Dam spillway. No uncontaminated runoff from these catchments will enter the overflow Dams Nos. 1 and 2 which will be used solely for I containment and disposal of overflow from the Eleanora Dam. During periods of bypass channel flow, Eleanora Dam may be replenished via the 600mm bypass pipe as currently I I I 31. I 4.0 EXISTING ENVIRONMENT
I 4.1 MINING COMPONENT
I 4.1.1 CLIMATE
I Rainfall and temperature data are available for Armidale, the recording centre which is nearest to the Comet gold mine and the township of Hillgrove. Records have I been kept since 1857. Seven years of evaporation data are available from a Class A Pan at the University of New England in Armidale. This first sub-section on climate is relevant to all three components. A rainfall intensity diagram has been utilised for I Hillgrove. The mean monthly rainfall and evaporation figures are graphically shown in Figure I 4.1-1. The mean annual rainfall is 793mm. There is a pattern of peak rainfall occurring during the summer months, between November and February and an autumn trough I during April and May. The annual mean class A pan evaporation is 1600mm with the summer rate approximately three times that of the winter rate. I Mean daily maximum and minimum temperatures per month are presented in Figure 4.1-2. Armidale experiences warm summers and cool winters. Windrose diagrams for the Armidale area are presented in Figure 4.1-3. The Lii observations were made at 9.00a.m. and 3.00p.m. during the period 1957 to 1986. Most frequently winds are from the west and with the next most common direction being the H east. A rainfall intensity diagram for Hillgrove is presented in Figure 4.1-4. This I diagram shows the probabilities of certain rainfall intensities occurring for various durations of time and at various average recurrence intervals. H 1 4.1.2 TOPOGRAPHY
The existing mine is located on the south-western slopes of Happy Valley, south of I Rockvale (see Fig 3-1). Surface contours of the site and its vicinity are shown on Fig 3-8. The two catchments which include the site drop from around 1120 A.S.L. at the top I of the surrounding ridges to approx. 1010-1020 m on Valley Creek. The site itself drops from ilOOm to around 1030m. I I I 32. I 4.1.3 SOILS I An initial soil survey was carried out in 1986 (Lewis Environmental Consultants, 1986). In addition, WLPU Consultants conducted a soil geotechnical survey of the I tailings storage area as part of the previous investigations for preparation of the previous EIS (Martin, 1988). This survey involved excavation and logging of 12 test pits I and collection of samples for subsequent testing. The soils on the site are derived from granite. On the ridges and steeper slopes the I soil prof ile generally consists of a greyish brown sandy loam A horizon grading to a yellow-brown sand and light yellow sand. The B horizon is a yellow clayey sand with some gravel. The A horizon ranges up to 150mm in depth and the B horizon extends from I 500 to 1,500mm depth. The soil profile overlies weathered granite.These soils are classified as Siliceous Sands (Great Soil Group) and Northcote Uc 1.42. I A composite sample of the A horizon from the siliceous sands was collected during the initial soil survey for chemical and physical analyses.The results of the analyses I were given in Appendices I and II of Martin (1988), respectively. The particle size analysis confirms the sandy nature of the top soil with 74% of the soil in the fine and P coarse sand fraction. The chemical analysis shows that the soil is strongly acidic and is deficient in a number of elements for satisfactory pasture growth. The soil is particularly deficient in nitrogen, potassium, sulphur, calcium, magnesium, copper, zinc, I boron and molybdenum. However, the levels of phosphorus in the soil are adequate for pasture growth. E In the drainage line, on lower slopes and in depressions of the site catena clay deposits and clay soils have developed. Soils in the drainage line near the north-west I boundary of ML 755 were classified as Yellow Earths and Gn2.21 (Lewis Environmental Consultants, 1986). These soils have a clay loam to medium clay B horizon under a I lighter textured A horizon. These soils are slightly acid with a pH of 6. On the lower slopes and in depressions, deposits of medium clay (more than 40% clay) with medium plasticity were identified during the geotechnical investigations. I These deposits had restricted drainage and were found to have a low permeability. I I I I I