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During the past decade, efforts to minimize the impact of mining on the environment have increased. Open pit mining for the raw material extraction of ores (e.g., copper-rich sulfide ores), impacts the surrounding landscape by the excavation activities and by the large remaining volumes of waste rocks and remains of processed ore after the extraction of precious metals like copper. Extracting copper directly from the ore in the subsurface would significantly reduce these impacts. The technology of in situ biomining is a promising candidate for this process1. This publication describes the use of stimulated microbial activity to extract the precious metals from the ore into an aqueous solution in the subsurface. Thus, a copper-rich solution can be easily pumped back to the surface to further concentrate the metal, for example.
The activity of ore-leaching acidophilic microorganisms has been studied in many laboratories for a diverse array of parameters2,3,4,5,6. However, pressure effects on the microbial activity resulting from the difference between ambient surface lab conditions (near 1 bar) and the subsurface at a depth of 1,000 m with hydrostatic conditions (~100 bar), are not well-documented. Therefore, the effects of pressure on microbial iron reduction have been investigated through different experimental avenues7. Here, the most suitable technique is described in detail.
High-pressure reactors have been used extensively to study reactions at pressures and temperatures occurring in the subsurface of the earth. Such reactors consist of a reactor vessel at the bottom that can contain a fluid sample with a microbial culture. Sitting on top of the reactor vessel, the reactor head offers a diverse array of connections and interfaces for safety measures and monitoring sensors (e.g., temperature or pressure). Most high-pressure reactors are made of stainless steel. This material offers high resilience and good machining properties, but the corrosion resistance of the stainless-steel surface is not adequate for every application. For example, if highly acidic or highly reducing aqueous solutions are investigated, significant reactions of the compounds of interest with the reactor wall may occur. One way to avoid this is to insert a liner into the reactor vessel, for instance a liner made from borosilicate glass7. It is easy to clean and can be sterilized by autoclaving. In addition, it is not attacked by acidic or reducing aqueous solutions. Even though a liner can help to prevent artificial reactions of the solution or microbes in the solution with the stainless-steel reactor wall, several problems remain. For one, if a corrosive gas is formed, such as hydrogen sulfide produced by sulfate-reducing bacteria, this gas might react with the uncovered surface of the reactor head sitting above the liner. Another disadvantage is that it is not possible to withdraw a sample from the reactor while maintaining the pressure.
To overcome these limitations, specialized flexible reaction cells inside the high-pressure reactors have been developed for a variety of applications. A flexible polytetrafluoroethylene (PTFE) cell8 was designed for solubility studies of salts in highly saline brines. However, the limitation of this system is that some gases can easily permeate the PTFE. In addition, this material still has a relatively low temperature stability. Thus, the system was improved by designing a flexible gold bag with a titanium head9 to be placed inside the stainless-steel high-pressure reactor. The gold surface is corrosion-resistant against acidic or reducing solutions and gases. The titanium surface is also highly inert when passivated thoroughly to form a continuous titanium dioxide layer. During sampling from this reaction cell through a connected titanium sampling tube, the gold bag shrinks in volume. The system's internal pressure is maintained by pumping the same volume of water, as is withdrawn by sampling, into the stainless-steel high-pressure reactor accommodating the reaction cell. The sample inside the reaction cell is kept in motion by rocking or tilting the high-pressure reactor by more than 90° during the experiment.
The reaction cell consists of the parts depicted in Figure 1: the gold bag, titanium collar, titanium head, stainless steel washer, titanium compression bolt ring, titanium sampling tube with stainless glands and collars for the high-pressure coned and threaded connections on both sides, and the titanium valve. The gold bag is a cylindrical gold (Au 99.99) cell with a wall thickness of 0.2 mm, an outer diameter of 48 mm, and a length of 120 mm.
All titanium parts are custom-made by the workshop from titanium grade 2 rods. The dimensions of the collar, head, washer, and compression bolt ring are visible in Figure 2. The titanium sampling tube is a capillary of titanium with an outer diameter of 6.25 mm and a wall thickness of 1.8 mm, resulting in an inner diameter of 2.65 mm. It is fixed into the titanium head and the titanium valve by high-pressure coned and threaded connections ensuring a seal of titanium-against-titanium surfaces. The high-pressure titanium valve is equipped with a slow opening stem to allow for very controlled opening or sampling even at high pressure. This system was used in numerous studies10,11,12.