


Vol 60, No 12 (2017)
- Year: 2017
- Articles: 8
- URL: https://journals.rcsi.science/1068-364X/issue/view/13953
Coal
Influence of the Batch Composition at AO EVRAZ NTMK on the Coke Quality and Pulverized-Coal Consumption
Abstract
The clinkering, coking, and lean components of the coking batch at AO EVRAZ NTMK are experimentally studied. On the basis of the laboratory coking of 67 versions of the production batch at AO EVRAZ NTMK, with different content and properties of the clinkering, coking, and lean components, the formation of the coke’s CSR and CRI values is analyzed. A mathematical model is developed for predicting the coke quality on the basis of the batch characteristics. The pulverized-coal consumption at the blast furnaces is predicted for wet- and dry-quenched coke produced from different batches at AO EVRAZ NTMK.



New Approach to Coal Preparation of Different Metamorphism Stage
Abstract
The dry beneficiation of coal samples at different metamorphic stages (lignite, coal, anthracite) is compared, before and after heat treatment. By thermal modification of the coal in the absence of air, the unit ash content (the ratio of the ash content to the heat of combustion) may be reduced by a factor of 1.3–1.6. In other words, the ash and slag formation on combustion may be reduced. Intense magnetic and electrostatic separation may be used for dry beneficiation of high-ash fine-grain coal. The removal of the mineral fraction by such methods is more effective after pyrolysis of coal stocks at different metamorphic stages.



Coke
Influence of the Crushing of Bituminous Batch on Coke Quality
Abstract
Laboratory and industrial research confirms that decrease in the clinkering properties of bituminous coal when it is present to excess in the coking batch improves the strength of blast-furnace coke. If coal batch containing >70% bituminous coal is crushed until its content of the ≤3 mm class is 90%, the crushability Π25 may be increased by 1.8%, with decrease in the susceptibility to wear И10 by 0.8%. This behavior may be explained in that increase in the specific surface of the coal particles reduces the fluidity of the plastic mass and hence increases its viscosity. Consequently, the residence time of the gaseous products in the plastic zone increases. That results in the formation of a large quantity high-molecular gas, creating higher expansion pressure. The overall outcome is greater utilization of the destruction products as plasticizers; the formation of additional liquid from the gaseous products within the grains; and improvement in the contact conditions.



Chemistry
Products of Coal Pyrolysis
Abstract
Solid, liquid, and gaseous products of the pyrolytic decomposition of coal are studied. Analysis of the gas composition shows that most gas is formed at 600–900°C. The calorific value of the gas is greatest at 500°C, on account of the high concentration of methane and heavy hydrocarbons. The results for the liquid products show that, with increase in temperature, the yield of phenols decreases, while the concentration of polycyclic aromatic hydrocarbons increases.



Flotational Enrichment of Coking Coal by Means of Spent Motor Oil
Abstract
The flotation of coking coal (metamorphic stages II–IV) by means of ozonized spent motor oil is considered. The ozonized oil exhibits high flotational activity with respect to coal of poor and moderate metamorphic development: Ro < 1.2%. Ozonization improves the selectivity of the motor oil in flotation by a factor of 2–3.



Tar Produced in the Coking of Rammed Batch
Abstract
The yield of tar and its properties in the coking of rammed batch is of particular interest in the light of the broader adoption of this technology. In laboratory reactors, the tar yield from rammed batch is lower than for unrammed batch. However, in industrial furnaces, the tar obtained in the coking of rammed batch is characterized by lower levels of pyrolysis. It is evident from analysis of the tar’s quality, viscosity, and group composition and also from granulometric analysis of the quinoline-insoluble components that the primary destruction products of the thermochemical processes in the coking of rammed batch react with the solid and liquid phases.



Organization of Production
Selecting the Target Transformations in the Design of Chemical Production Systems
Abstract
The design of production systems at chemical plants is considered. Attention focuses on the selection of the target transformations of materials within a virtual system. The information approach is adopted in an algorithm for step-by-step selection of the target processes and their optimal integration within the virtual system. The key feature of this algorithm is that it allows to use general principles for the distribution of the system’s functions between its elements and subsystems to ensure optimal integration of the target processes. Those principles were described in previous works. As an example, the algorithm is employed in the optimal organization of a system for converting lignite to synthesis gas, with specified proportions of the key components.



Environmental Protection
Fire and Explosion Risks of Glycol-Based Vapor–Air Mixtures
Abstract
@Abstraction limits of flame propagation are determined for 13 glycols, as well as their enthalpy of formation and enthalpy of combustion. These characteristics depend on the number of carbon atoms in the glycol molecule. The combustion parameters are calculated for vapor–air mixtures of glycols and monoatomic alcohols, in the case where P = 1 atm and V = const. The adiabatic combustion temperature of mixtures of limiting and stoichiometric composition does not depend on the number of hydroxyl groups in the alcohol molecule. The explosive pressure of glycol is slightly higher than for monoatomic alcohols.


