


Vol 60, No 2 (2017)
- Year: 2017
- Articles: 7
- URL: https://journals.rcsi.science/1068-364X/issue/view/13934
Coal
Changes in lignite on industrial storage
Abstract
The composition and properties of Kemorovo lignite are studied. Lignite is characterized by high moisture content and yield of volatiles, high chemical activity, and a high content of micro- and mesopores. The moisture absorption and moisture loss of lignite (piece sizes 3–8, 8–12, 12–25, and 25–50 mm) are studied as a function of the contact time with water and air. Industrial data are presented for the lignite temperature on storage in the batch yard at AO Kuznetskie Ferrosplavy. When a probe is introduced in the coal to depths of 400–1000 mm, its temperature varies from 68–78 to 78–90°C. With increase in holding time, it rises to 83–93°C. Recommendations are made for refinement of the technical instructions regarding lignite storage.



Changes in the petrographic composition of coal batch on crushing
Abstract
The influence of crushing on the maceral composition of coal is studied. The experimental data indicate not only redistribution of the petrographic microcomponents by size but also change in the maceral composition, depending on the intensity of grinding. With increase in the degree of crushing from 55.5 to 96.2%, the vitrinite content in the batch declines from 70 to 63%, while the total content of fusinized components increases from 29 to 35%. For coal with 50–80% vitrinite, which is less strong than coal with smaller vitrinite content, crushing is probably accompanied by disruption of the molecular interactions and rupture of the chemical bonds in the organic macromolecules. That leads to partial destruction of the brittle vitrinite structure, especially in the intermediate stages of metamorphism (Ro = 0.9–1.39%).



Coke
Improving the performance of dry-quenching units by minimizing coke losses
Abstract
In assessing the operational efficiency of dry-quenching units at coke plants, it is important to consider the coke losses. In the present work, existing methods of determining the coke losses are analyzed. The method selected is based on continuous measurement of the flow rate and composition of the excess circulating gas released from the dry-quenching unit; it is compatible with different coke-discharge systems. Methods of determining the productivity of the dry-quenching unit are assessed. Means of reducing the coke losses are discussed.



Optimal heating system organization in coke ovens
Abstract
In optimizing the organization of the coke oven’s heating system, the feasible region of parameter values is identified and analyzed. Previous research has shown that optimal organization of the heating system calls for the forced recirculation of gas fluxes with recirculation rates exceeding those currently employed and also for measures that simultaneously permit energy conservation and curb nitrogen oxide emissions. To that end, the influence of recirculation on process parameters is analyzed in the present work, and the feasible region is found on the basis of the following constraints: no reduction of heat supplied for the coking process; and unchanged consumption of coke-oven gas. In addition, the basic parameters of the power generation subsystem are determined by assessing the energy balance.



Chemistry
High-temperature synthesis of pitch
Abstract
The heat treatment of the anthracene fraction of coal tar under pressure is considered. In the production of synthetic pitch, the duration of the process is varied from 10 to 80 min, at a temperature of 500°C and a pressure of 3 MPa. Kinetic data for the formation of γ and α1 fractions show that the polycondensation of the γ fraction is of second order, while the formation of the α1 fraction is of zero order. Pitch obtained with holding for 10–40 min does not contain the α1 fraction. Extending the process beyond 30 min does not affect the removal of heteroatoms. IR spectroscopic data indicate that dealkylation predominates for the first 40 min. Then the process slows, and compaction develops.



Utilization of Production Wastes
Processing of converter slurry by coking with coal
Abstract
Processing of the industrial waste formed at steel plants is of great importance. In the converter production of steel, 12–25 kg of fine dust is formed in the production of 1 t of steel, depending on the composition of the raw materials, the furnace design, and the smelting conditions. Wet cleaning of the waste gases converts the dust into a slurry containing 46–50% Fe2O3. It is difficult to process such slurry because of its high water content, the small particle size, and the presence of zinc oxides. Standard dehydration technology is complex. It is also associated with thermal drying, which poses an explosion risk, while briquetting or granulation does not resolve the problem posed by the presence of zinc oxides and is complicated by a lack of acceptable binders. Researchers at Siberian State Industrial University have developed complex conditioning of iron-bearing slurry by nonthermal adsorptive dehydration and subsequent thermochemical agglomeration, with simultaneous reduction of the iron and zinc oxides. Adsorptive dehydration to a moisture content of 2‒3% is possible by contact with porous lignite semicoke produced by Termokoks technology. Then the lignite semicoke is pneumatically separated and sent for use in energy systems, while the iron-bearing product is mixed with GZh or Zh coal and sent for thermooxidative coking in a furnace of special design (an annular furnace with a rotating hearth), where large and strong pieces of ferrocoke are obtained at 1050–1100°C. The ferrocoke contains 55–60% of the iron-bearing product. The oxides of iron and zinc are almost completely reduced. The zinc passes to the vapor phase and is removed with the combustion products of the volatile coking components. On cooling to 850°C, the zinc vapor condenses. The ferrocoke obtained is suitable for blastfurnace use, thereby reducing the consumption of sinter and coke. The heat obtained on cooling the ferrocoke and the energy of the combustion products after the deposition of zinc are utilized in a gas-turbine system.



Sorptional properties of fuel shale and spent shale
Abstract
The sorptional properties of fuel shales and spent shales in removing organic compounds (petroleum and its derivatives) from water are studied. The basic benefit of spent shale as a sorbent is that it is available at no expense as the processing waste of fuel shale. After sorption, the fuel shale or spent shale saturated with petroleum or its derivatives may expediently be used as a fuel, on account of their high calorific value.


