Fig. 1 Schematic diagram of the laboratory installation: SVR – single-phase voltage regulator, RC – resonant converter, VT – voltage transformer, DR – diode rectifier, VPG – voltage pulse generator, CGC – crushing and grinding chamber
Рис. 1 Принципиальная схема лабораторной установки: SVR – однофазный регулятор напряжения, RC – резонансный преобразователь, VT –трансформатор напряжения, DR – диодный выпрямитель, VPG – генератор импульсов напряжения, CGC – камера дробления и измельчения
In experiments on grinding rocks, sieves with cells of 15 and 5 mm were used as a grounded electrode. When exposed to pulp of rock, instead of sieves, a metal bowl with a hemispherical shape of the inner side was used. After several initial pulses, the pulp shrunk, so the length of the working gap changed once, but most of the pulses were applied at a constant set length of the gap.
Electric pulse impact on rock samples was carried out at the maximum energy parameters of VPG. This approach was due to the fact that the electrical properties of some rock samples were not known. The operating design and energy parameters of the installation are shown in Table 1.
Table 1 Operating parameters of the lab EPD installation
Таблица 1 Рабочие параметры лабораторной установки для электроимпульсной дезинтеграции
When conducting experiments with pulp of rock, the voltage at the load and the current through the load were measured using a resistive voltage divider and a current shunt.
The crushing experiments were carried out in several stages. A fraction less than 2 mm was taken as the minimum fraction in the classification of crushing output products. The experiments were completed when fractions less than 0.25 mm and less than 0.5 mm were separated from the total amount of fractions less than 2 mm from all stages for comparison with control samples. Control samples: 1. Iron quartzites of medium crushing; 2. Finely crushed ferruginous quartzites; 3. Pulp after fine crushing; 4. Apatite-nepheline ore of medium crushing; 5. Apatite-nepheline ore of fine crushing; 6. Apatite-nepheline ore pulp Figure 2 shows typical oscillograms of the processes of electric pulse action on pulps of ferruginous quartzites and apatitenepheline ore. The difference in the shape and magnitude of the voltage indicates the high conductivity of the pulp, while the pulp at the initial moments of time exhibits dielectric properties, which explains the delay in the breakdown of the gap by 0.6 μs.
Fig. 2 Oscillogram of voltage and current during breakdown of gaps with pulp
Рис. 2 Осциллограмма напряжения и тока при пробое зазоров с пульпой
The masses of rock samples for electric pulse action were selected based on the amount of available large-sized material. The specific energy costs for electric pulse disintegration were calculated in relation to the mass of the useful fraction without taking into account the non-crushed material. Experiments on electric pulse disintegration were divided into 3 stages: 1. Electric pulse disintegration of rocks on a sieve +15 mm (Table 2); 2. Electric pulse disintegration of rocks on a +5 mm sieve with a decrease in the working gap in the crushing and grinding chamber to a critical length of 30 mm, after which the electric pulse action turned into electrohydraulic (Table 3); 3. Electric pulse disintegration of rocks was carried out on a 2 mm sieve, fractions –5 + 2 mm on a 5 mm sieve. Crushing was carried out until the critical length of the working gap in the chamber was reached (Table 4).
Table 2 Sample weights and energy costs for EPD on 15 mm sieve
Таблица 2 Масса образцов и затраты энергии на электроимпульсную дезинтеграцию на сите 15 ммTable 3 Sample weights and energy costs for EPD on 5 mm sieve
Таблица 3 Масса образцов и затраты энергии на электроимпульсную дезинтеграцию на сите 5 ммTable 4 Sample weights and energy costs for EPD on 2 mm sieve
Таблица 4 Масса образцов и затраты энергии на электроимпульсную дезинтеграцию на сите 2 мм
Below in Table 5 are the results of chemical analysis of samples of rocks, ores and pulps of mining and processing plants before and after electric pulse disintegration. Additional output of useful components from rock samples after electric pulse disintegration are indicated as a percentage of mass.
Table 5 Chemical analysis of rock samples of mining and processing plants before and after EPD
Таблица 5 Химический анализ образцов горных пород горно- обогатительных комбинатов до и после электроимпульсной дезинтеграции
The obtained results of the conducted research and development made it possible to confirm the possibility of obtaining an additional yield of a useful component from rocks, ores and pulp of mining and processing plants after their electric pulse processing in comparison with control samples that were not subjected to electric pulse effects.
The results of the chemical analysis presented in Table 5 showed that after the electric pulse disintegration of the rock samples of mining and processing plants, the percentage of release of useful component such as Al2O3, Fe, Fe2O3, FeO, P2O5, depending on the fraction and the stages of rock crushing (large, medium, fine, pulp) can be increased by 7.59% and up to 113.79% respectively.
Mineralogical analysis of samples showed an additional yield of chemical elements such as SiO2, TiO2, MnO, CaO, MgO, K2O, Na2O, SrO, F, SO3. After electric pulse processing of rock samples, the yield of useful components can be increased by 9.07% and to118.3%.
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