Application of Thermal Fragmentation in Australian Hard Rock Underground Narrow-Vein Mining

This paper presents the results from the investigation of the application of thermal fragmentation in Australian hard rock underground narrow-vein mining. Two geologically similar samples from an underground narrow-vein hard rock gold mine were collected to obtain a measure of the technology’s ability to recover ore by the creation of large thermal openings to assess the applicability of the thermal method. Particle size distribution showed a higher generation of fine product, − 2 mm, by thermal fragmentation compared with selective blasting by 31%. The Bond work index for thermal ore (12.62 kWh/t) is half to that of the blasted ore value (25.32 kWh/t). The average grindability obtained for the thermal ore sample was greater than the blasted sample by a factor of 2.44, a higher value indicating a decrease in the energy required to grind. The thermal fragmentation method generates product with higher dissolution of gold in cyanide, by 14% for the − 9.5 + 2 mm size fraction samples. Additionally, the thermal fragmentation results in higher production of − 9.5 + 2 mm material by 15 % compared with selective blasting.


Introduction
The profitable extraction of valuable minerals from orebodies forms the main objective of any mining enterprise. Both, open pit and underground, minings are profitable only when the revenue exceeds the costs of extraction and refinement of a saleable product.
Narrow-vein type deposits are particularly challenging to mine profitably. A definition of a narrow-vein deposit is an orebody less than 3 m average thickness. Narrow-vein systems have historically represented an important source of the world's exploitable gold, silver, tin and uranium [7], but have proven problematic to mining companies due to the complexities inherent to these deposits. These complexities include but are not limited to their predisposition to erratic grades, often attributed to the nuggetty distribution of gold throughout the system and its complex geology, resulting in difficulty of estimating resources [8].
These complications result in narrow-vein systems being high-risk investments and as such, it tends to be difficult to raise funding for both exploration and exploitation of these deposits. Narrow-vein systems are generally low tonnage and expensive to mine, mainly due to the work force requirements during both the development and production cycles of mining [9]. Additionally, conventional extraction methods often result in significant dilution of the ore, and there are substantial limitations pertaining to the mechanisation of the extraction process. The costs associated with the development of narrow-vein deposits is largely similar to those of a bulk mining operation, but as these costs are distributed over lower tonnes at variable grades [9], the extraction of the targeted material must be economical or beneficial to the overall mining operation.
Mining operations in most instances consist of two distinct subsystems, the mine and the processing plant. The focus of significant work in the field of mine-to-mill optimisation [10,17,18] is the adjustment of one or both subsystems in order to obtain an optimum set of variables for the overall mining operation. A suggested approach to achieving this optimisation is improvement of the blasted fragmentation of the run of mine ore rock. The goal is to produce a fragment size distribution that would minimise overall mining and processing costs [17].
The processing plant consumes a large portion of the energy supplied to a mine site. When processes in the plant include crushing, grinding, flotation, concentration and leaching of the ore, that portion can increase to approximately 82% of total energy requirements [16]. In most instances, comminution circuits account for the greatest fraction of expended energy in the processing plant and can range from 30 up to 73.5% [11,21]. A reduction in the costs of comminution would therefore be an important step to produce savings for a mining operation. These potential saving (Table 1) values will vary depending on the hardness of the ore as well as the grain size characteristics [21].
Therefore, in order to achieve an energy efficient operation; firstly, production of fine material during blasting or during the primary breakage method should be maximised, and secondly, a reduction of the quantity of processed tonnes required to produce a final product would prove to be economical.
Generation of a relatively fine primary mining product is achieved by high intensity blasting, employing the low cost energy of explosives. High intensity blasts, when effectively controlled, transmit a large fraction of the useful energy into the particle size reduction of the blasted rock.
The difficulty encountered when increasing the explosive energy in a confined area, such as a narrow vein of ore, is that the transfer of the energy contained in the explosive to the target material is not 100% efficient. This excess explosive energy can result in breakage of the surrounding wallrock, adding additional tonnes that dilute the ore sent to the mill and can destabilise the working area, consequently increasing the costs of ground support. Minimising the tonnes processed to provide an economic final product requires a high level of selectivity in mining.

Thermal Fragmentation
The fragmentation method proposed in this study consists of a strong burner (Fig. 1) powered by diesel fuel and compressed air of approximately 115 mm diameter. The process involves inserting the burner into a 152 mm diameter pilot hole, drilled by a longhole drill. The burner is located at the toe end of the hole and is ignited. The in-hole temperature can rise up to 800°C , and this thermal stress creates a spalling effect [15], causing individual grains within the rock on the outermost surface of the drillhole to expand and contract depending on their own inherent thermal expansion factors. When the thermal expansions of adjacent grains in a rock vary sufficiently, intergranular fracture occurs; reducing particle cohesion and the subjected particles tear away from the coherent wallrock [5]. This spalling allows for the expansion of the pilot hole cavity, increasing the diameter of the hole from the drilled from 152 mm to a maximum of 1200 mm by the simple action of leaving the burner in a particular part of the hole for a given duration of time. The durations vary depending on the geology of the rock and are site specific. Narrow excavations of 250-450 mm require short residence time of 5-10 min, and larger excavations require up to 15-25 min. Once the time has elapsed, the burner head is retreated out of the opening for about 600-900 mm to continue the thermal process on the next slice of the vein (Note: These are approximations based on the use of thermal unit in an underground Australian hard rock mine). The process continues until the burner head becomes proximate to the collar of the pilot hole, and then the thermal unit moves to its next hole.
The rock fragments produced are removed by a vacuum. This vacuum system creates a pressure seal around the collar of the pilot hole, removing both fragments of rock and any exhaust fumes from the burner, ensuring no fumes or gases are vented into the working area.
The process produces fragments of < 13 mm in size which are transported by means of the vacuum system to a stockpile for loading or directly to a haulage vehicle. The product size of thermal fragmentation largely eliminates the need for primary crushing (Fig. 2), producing a material more suited for fine grinding.
During vacuuming of the hole, the particles are injected with a stream of water to prevent the overheating of the transmission pipes by the quenching of the heated ore; this also aids the transmission by fluidising the ore.

Applications of Thermal Fragmentation
In underground mining, a considerable interest exists in nonblasting methods of extraction, especially in built-up areas such as those in the Victorian goldfields in Australia [14]. In respect to the underground mining of narrow veins in hard rock, thermal fragmentation provides a degree of competition to the methods generally relied on for the extraction of ore, such as longhole open stoping, shrinkage stoping, cut-and-fill and resue mining. Longhole open stoping is suited for the extraction of steeply dipping veins of width exceeding 1.5 m and provided the continuity is substantial, could prove more practical option to mine a deposit of this nature [12].
Shrinkage stoping is suited to deposits steeply dipping and of width less than 1.5 m. Dilution, safety and manpower become variables worth consideration when deciding the application of this method. Blasting breaks the rock and this encourages dilution of the ore. Drilling of blastholes for this method often is completed from the top of previously broken ore by pneumatic airleg drill. Skilled manpower is a vital component of this method, airleg operation is a strenuous job, which is generally done from on top of an unconsolidated ore rock pile. This method presents some safety risk, and the requirement for skilled labour accounts for up to 40% of the costs of mining [7].
A benefit of the application of thermal fragmentation on a vein of the same characteristics is a two-man crew that is required for the operation of the thermal unit, and the fragmented ore is largely removed from the hole during operation. Drilling of pilot holes for thermal fragmentation constitutes the only additional requirement for manpower during mining.
For resue mining and cut-and-fill mining, controlled blasting practices could be utilised to minimise dilution; delays in the mining cycle will be encountered during both the split face firing of the waste and ore and whilst filling during cut-and-fill mining. Increased cycle time often results in losses in production and therefore profit. Due to this, alternative methods may be sought to extract the ore without delays.
Utilisation of thermal drilling may prove more economical for the extraction of the narrow vein of ore. The high selectivity of the method in consort with the production of a primary mining product of reduced size would result in mitigated haulage costs and decrease the volume of ore requiring crushing. Any assessment of the viability of this process must also take into account the increase cost per tonne inherent to thermal fragmentation.
A cost comparison was completed by Rocmec International Inc., between longhole open stoping and thermal fragmentation ( Table 2) [15]. From the table, the unit cost $113.50/t for thermal fragmentation is significantly greater than $19.50/t for longhole open stoping. The example takes into account the substantial difference in dilution between the processes, resulting in the extraction of 12,645 tonnes of additional reserves in the longhole method to produce a similar number of ounces. Table 3 illustrates the significance of extracting only profitable material during a mining operation. The estimated thermal fragmentation unit mining cost per tonne is 6 times greater than that of the longhole method, but in this example, the thermal process produces an ounce of gold at a discounted rate and therefore generates a greater profit margin.
Comminution benefits accrue from treating rock fragmented by thermal stress due to a reduction of both feed tonnage and particle size of the feed for further processing. Reduced run of mine (ROM) tonnage to the mill decreases energy requirements and results in reduced wear on the comminution equipment. With the production of a finer primary mining product, elimination or substantial reduction of the existing initial coarse stage of particle size reduction can be realised. Overall comminution energy savings are then realised as defined in a study concerning fine grinding in respect to a decrease in grinding feed size [21].
The substantial thermal stress applied during the process is analogous to thermal preconditioning that has been Fig. 1. a Thermal fragmentation burner head [15]. b thermal burner flame [4] Fig 2. Thermally fragmented rock [4] investigated since the 1920s. Such studies were summarised by Tavares & King; they concluded that improvements to the efficacy of the comminution circuit existed when a mill feed material is subjected to a sufficient degree of thermal preconditioning.
The effect of thermal pre-treatment of brittle material on the breakage characteristics of a treated rock is attributed to the differential thermal expansion of adjacent grains, is not associated with the rate of heating and is independent of the number of heating cycles applied [5], merely due to the temperature of thermal expansion. During experimentation, Brown, Gaudin and Loeb Jr found that heat treatments up to 700°C have varied levels of effect on the breakage characteristics of samples of granite, and that further increases in temperature up to 1000°C had a limited effect [6]. Heat treatment of quartz samples by Tavares and King followed by subsequent water quenching showed a reduction; the required energy for fracture by at least 55% in the particle size interval of 0.7-5 mm. This effect, caused by the heat treatment and quenching, was enhanced in the finer particles [19]. Given that the thermal fragmentation process incorporates quenching of the As the thermal fragmentation breakage mechanism involves differential expansion of adjacent grains of the rock structure, applying the process to structures containing minerals of different composition (e.g. quartz and gold) could elicit liberation of the gold. Because liberation of the valuable component of the ore from the gangue is the objective of size reduction operations [6], thermal fragmentation may provide additional opportunity for energy savings in the processing plant. If a liberation effect eventuates from the thermal stress, ultra-fine grinding could be reduced if not eliminated from the treatment process.
Thermal fragmentation technology has been employed in a number of countries since its conception and consequent development into a viable narrow-vein mining method. During the period of 2009-2010 [1][2][3], thermal fragmentation technology was deployed at Great Basin Gold's Hollister mine, NV, USA; Newmont's Midas mine, NV, USA and Fresnillo La Cienega mine, Mexico. In 2014, exclusive distributorship agreements were established with Maxem Holdings for South Africa and NDR for distribution of the technology in Japan.

Material
In order to incorporate the thermal fragmentation into Australian mining operations, a series of tests were undertaken to demonstrate the process and to test the performance of the new technology under Australian mining conditions by Safescape, a mining contracting company.
One of the trials took place in an underground narrow-vein hard rock gold mine, approximately 50 km northeast of Melbourne. A number of pilot holes were drilled, both directly into the gold bearing quartz veins and into the host rock to obtain a measure of the technology's ability to create large thermal openings for assessing the applicability of the thermal method in creating the excavations required for the installation of their laddertube systems.
Two economical grade gold ore samples were collected to perform assessment and comparison of the products generated using the two approaches. One sample, thermally fragmented  ore, generated from a narrow section of reef and the second from selective blasting a small stope of the same reef. Approximately 800 kg (2 × 44 gallon drums) of thermally fragmented ore and 1500 kg (4 × 44 gallon drums) of blasted ore samples were received, and representative samples were generated by cone and quartering for both ores.

Methodology
The particle size distributions of the thermal and blasted ores were generated by a measure of the retained masses on shaker screens following the generation of a representative sample of the ore.
For the thermal ore, due to its narrow size distribution, the total sample was coned and quartered in order to obtain a tentative size distribution. From this, the 95% passing size was obtained and used to formulate the representative mass by means of Gy's sampling theory formula [20]: where M is the minimum mass of sample, g; d is the screen size that retains coarsest 5% of material, P95 cm; s is the statistical sampling error and C is the sampling constant for the material sampled, g cm 3 Once formulated, the mass was obtained by cone and quartering the recombined sample.
Due to the volume and broad size distribution of the blasted ore, generation of a tentative size distribution would prove difficult, and therefore the use of the Gy formula would not be feasible. Due to this, a size distribution was completed on the 1500 kg sample.
Gravity concentrates of five size fractions (+ 9.5 mm, − 9.5+ 2 mm, − 2 mm + 1 mm, − 1000 + 300 μm and − 300 μm) of both ores were assessed for the gold liberation. The degree of liberation on the + 9.5 mm material was visually analysed. The samples were wetted to increase reflectivity and manually inspected. Optical microscopy was used for testing gold liberation in samples − 9.5 mm.
Each of the size fractions (+ 9.5 mm, − 9.5 + 2 mm and −2 mm) of the thermal fragmentation and selected blasted samples were analysed for cyanide leachable gold content. Solid residue from the cyanide leachable test was analysed for gold by fire assay. The tests allow to determine the amount of gold leached by cyanide and total gold content of a sample.

Sample Size Analysis
Particle size distribution data generated for the thermally fragmented and blasted rock samples displayed the significant difference in breakage behaviour between the methods (Fig. 3). The blasted rock was shown to possess a broad spectrum of sizes, 54.9% of which was reported to the coarse size fraction. The thermal sample demonstrated a tendency for material to fragment in the − 9.5 + 2 mm fraction ( Table 4). The thermal process proved more proficient at generating fines, with an additional 15.9% reporting to the fine particle size fraction.
The results show that 23.96% and 12.50% of the total masses, for thermal and blasted products, respectively, reported to the − 4.75 + 2 mm screen (Table 5), representing the greatest accumulation of either product on a single screen. Thermal fragmentation resulted in 1.9 times the percentage of particles retained at this size, re-enforcing the understanding of the intergranular  4 Changes in size distribution sought through blasting [17] fracture breakage mechanism attributed to differential thermal expansion due to thermal stress. Thermal fragmentation achieves the two objectives stipulated by Scott, Kanchibotla & Morrell; it reduced the top size of the material and increased the proportion of fines (Fig. 4). Their approach involved the optimisation of blasting practices at an increase in unit mining costs.
The size characteristics sought by blast optimisation in Fig.  4 are evident in the representation of the size distributions of the blasted and thermal products in Fig. 3. A reduction in the top size and an increase in the production of fines can be observed.
The influence of the selectivity and the product size characteristics of this process can be investigated in a rudimentary comparison of the costs associated with the extraction and initial comminution of a narrow vein of ore.

Rudimentary Cost Comparison of Reduction Processes
Using the method comparison by Donald and Jean-Phillip Brisebois (Table 6), an estimate of the produced fragmented rock can be extrapolated using the tonnages produced in their method comparison and the retained mass fractions of the blasting and thermal processes.
This analysis assumes that the blasting and thermal breakage characteristics obtained during completed research will be consistent with those encountered, investigated in the presented comparison (Table 7).
Production reduction costs are evaluated for a primary cycle through a comminution circuit using the theoretical mass distribution and the reduction cost per tonne for crushing and grinding (Table 8) [18].
The comminution costs in Table 9 were generated with the supposition that the fragmented material above 2 mm would report to a crushing circuit costing $0.75/t, and material passing 2 mm would report to grinding costing $3.75/t. This comparison shows that mining by means of thermal fragmentation is 82.9% less cost-intensive due to the reduction in sample size attributed to the selectivity of the process and the product particle size. Further comminution of the products would invariably result in additional savings due to the considerable difference in mined tonnes that would require crushing. This is due to the observed inefficiency of grinding relative to crushing, requiring 10 times the energy to grind the same volume of ore.

Bond Work Index
The Bond work index is used to calculate the grindability of ore and to postulate processing plant design. The Bond grindability test can be utilised to determine the difference in comminution energy requirements for traditionally blasted ore and thermally fragmented ore.
Comminution is an energy intensive process and represents relatively high operating cost and high capital expenditure. Thus, improvements in comminution performance is essential to support cost reduction, and estimation of the required energy assists to streamline the process of designing mining operations. Energy consumption models have been developed, including the Bond grindability test. First developed in the late 1920s by Fred Chester Bond, the Bond grindability test is the most well-known method and is used worldwide [13].
Both samples used in this test, thermally fragmented and blasted ore, were from the same mine site and are considered to be identical in terms of mineralogy and genesis. Therefore the method of extraction should be the only variable on the breakage characteristics of each ore type.
The grindability data, in conjunction with a number of equations formulated for the Bond work index calculation where P i is the mesh of grind size, μm (106 μm used); P 80 is the 80% cumulative passing of product, μm; F 80 is the 80% cumulative passing of feed, μm and G is the grindability, grammes per revolutions (gpr).
Bond work index testing supports the conclusion that the thermal stress applied to the rock during fragmentation and the subsequent quenching elicits a preconditioning effect on the ore. The obtained values for the product work index allow for the calculation for the energy input required to reduce the given samples.
Actual work: where W i is the Bond work index; P 80 is the 80% cumulative passing of product, μm and F 80 is the 80% cumulative passing of feed, μm.
An example was formulated with relevance to the size distribution data, showing the actual work input required to reduce a tonne of each mining product from its respective 80% passing size to an 80% passing size of 2 mm. Results (Tables 10 and 11) showed that reducing the blasted rock from 41 mm at its Bond work index of 25.32 kWh/t required 2.5 times more energy than reducing the thermal sample from 14 mm. These findings also would influence the cost comparison completed previously ("Rudimentary Cost Comparison of Reduction Processes" section), significantly reducing the cost of comminution of thermal rock relative to that of an equal volume sample of blasted rock. An observation can be made from the average grindability values obtained from the Bond Index Test work (Table 12), that the average grindability obtained for the thermal ore sample was greater than the blasted sample by a factor of 2.44, a higher value indicating a decrease in the energy required to grind.
The Bond work index grindability tests were completed in a single time for each sample in order to obtain an understanding of the relative difference in the reduction energy requirements between the primary rock breakage methods. The evaluation of the Bond work index of a material is a comprehensive process, requiring multiple stages of grinding to obtain a mean grindability. Several grindability tests are often required to obtain a true representation of a material's Bond work index and because of this, the Bond index values obtained may be subjected to inconsistency due to the single grindability test evaluation of the Bond work index.
Test work was completed with the assumption of a relatively equivalent geological composition between the samples, and this hypothesis is encouraged by the identical size distribution characteristics of the samples grinded for the Bond work index feed. The size distribution profiles of the undersize material also endorse this supposition, indicating uniformity of breakage behaviour, independent of the method of extraction. This identical breakage behaviour can be attributed to the relatively equivalent geological composition between the samples. Unfortunately, consistent or uniform geological conditions are not a guarantee in mining, and this may also contribute to variance in Bond Work Index.

Gold Assays
The results of the test work (Tables 13 and 14) show that coarse particle fraction (+ 9.5 mm) contains similar amount of gold, around 45%, available for cyanide leach for both thermal and blasted sample. In size fraction − 9.5 + 2 mm, dissolution increased up to 83% and 69% for the sample generated by thermal fragmentation and selective blasted sample, respectively. Therefore, 17% of gold of thermal sample and 31% of blasted material of this particle size range is not dissolved due to gold having no access to leachate. Even fines (− 2 mm) demonstrate comparable gold leachability, 92% for thermal and 90% for blasted material, production of the fine material is 16% greater for the thermal fragmentation method. The thermal fragmentation method generates product with higher dissolution of gold in cyanide, by 14% for − 9.5 + 2 mm size fraction. Additionally, the tests show higher production of − 9.5 + 2 mm material by the thermal fragmentation, 41%, compared with selective blasting method of breakage, 25.9% (Table 4). It is reasonable to conclude that the thermal fragmentation breakage mechanism promotes breakage along adjacent grains of gold and gangue which increases access of the valuable to leachate and as result enhances dissolution of gold.

Microscope Work
Visual and optical microscopic examination of gravity concentrated samples, thermal and blasted, at + 9.5 mm, − 9.5 + 2 mm and − 2 mm was performed.
There was no liberation of gold from the host rock identified in + 9.5 mm and − 9.5 + 2 mm size fractions of both samples, thermal fragmented and blasted sample. As can be seen from Fig. 5, visible gold is present with quartz in the size fraction of − 9.5 + 2 mm.
The samples analysed under the microscope showed significant liberation of gold below 300 micron. In the size range of − 1000 + 300 micron, it appeared that liberation of gold was largely complete in the thermally fragmented sample, whereas in some cases the blasted rock gold particles still possessed gangue minerals. It was observed that a large degree of gold mineralisation was occurring in the host rock as opposed to the quartz, this could impact the mining width selected for extraction. No significant trend was observed concerning a tendency for one product to become liberated at a courser size than the other.
The only evidence for free gold particles was found in material less than 2 mm (Figs. 6, 7 and 8).

Conclusions
The current study indicates the different effects of the thermal fragmentation and selective blasting methods on the property of the product generated from the Australian hard rock underground narrow-vein mining. However, this study is very limited due to the number of samples and the fact that it is single site-specific. As such, it cannot be definitively stated that the results are representative of the Australian mining industry. Further work from other sites would be needed to prove the results from this study can be replicated across other mines and other mineral commodities.
For the study, undertaken investigation of the primary mining products from both methods show substantial financial benefit can be theoretically obtained due to the size and breakage characteristics of thermal process. Due to the increased selectivity of the thermal process, less tonnes need to be generated to mine a narrow width of ore, increasing the financial benefit of this method of extraction. Degree of liberation and availability of gold for dissolution findings are significant in influencing the applicability of this process.
Further research trials and analysis will serve to reinforce the benefits of this mining method.