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Natalia Vasilievna Fedorova, Vasily Alexandrovich Mokhov, Elena Alexandrovna Krivobok
Platov South-Russian State Polytechnic University (NPI) Correspondence address: 132, Prosvescheniya St., Novocherkassk, Rostov region, 346428
ABSTRACT: Russia's energy policy for the coming years provides for greater use of coal fuel, combined with the introduction of non-waste technologies of its combustion. Russia has taken to burn coal with ash content of various indicators, including those of high. The question of efficient use of coal in thermal power plants (TPP) of Russia by his deep preparation for burning is considered in this article. One way to solve of this problem is the construction of modern coal preparation factory directly or near the power plant. The criteria of efficiency of coal combustion are systematized. The modern methods of mineral raw materials enrichment used in the mining, metallurgical and chemical industries are considered. The parameters of coal preparation equipment offered in the Russian market by manufacturers from different countries are investigated. The systematic analysis of production processes in the TPP by functional modeling techniques based on IDEF0 diagrams and hierarchies analysis of T. Saaty is performed, allowing to prove the correctness of the proposed solution of the problem of coal enrichment in TPP prior to combustion and to provide an option of the technological chain of operations performed. The technical and economic effect after object modernization is defined. Coal deep preparation for burning, including the introduction of coal preparation factory on TPP, will create the environmentally friendly technology of fuel and energy coal-fired complex.
KEYWORDS: high ash content coal; coal preparation; activation of combustion; analysis of technological processes; systems analysis; process modeling; ratingDownload this article as:
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Fedorova N. V, Mokhov V. A, Krivobok E. A. Functional Simulation of the Method for the Coal Preparation for Combustion in the Thermal Power Plant. Biosci Biotechnol Res Asia 2015;12(3)
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Fedorova N. V, Mokhov V. A, Krivobok E. A. Functional Simulation of the Method for the Coal Preparation for Combustion in the Thermal Power Plant. Biosci Biotechnol Res Asia 2015;12(3). Available from: http://www.biotech-asia.org/?p=3870>
Russia’s energy policy  provides for greater use of coal fuel, combined with the introduction of non-waste technologies of its combustion.
According to the Russian National Standards, the ash-content of coking coal shall not exceed 5-6%, and the ash-content of the steam coal shall amount to 13-18% [2-3]. The reduction of the ash content of the coal (coal preparation), supplied for the burning, should be based on the feasibility study and be profitable for the electricity and heat manufacturers.
Since the end of XX century the systematic analysis has become the main approach to solve the complex problems. Its application is the basis for a logical and consistent problem detection and validation of the proposed solutions. One of the modern tools of systems analysis for solving the problems of reengineering is a functional simulation using the appropriate computer technology and software . The validity of the application of the functional simulation technology, in particular, is confirmed by ISO 9000 Standards.
Common approaches to coal combustion in the Russian Federation and in the world
According to the first approach, the coal preparation is inefficient, since modern thermal power plant boilers are able to use coal of any quality index. According to the second approach, the feasibility of coal preparation is justified by the increase in TPP electricity production efficiency and depends on many specific factors: the ash and sulfur content, the fuel, transport and coal preparation costs, the environmental protection standards, performance and availability of boilers, etc. .
In Germany the combustion of coal with ash-content greater than 2%, is prohibited by the Law. Nowadays, in all industrialized countries 70-90% of all mined stone coal is subject to coal preparation: in the FRG – 95%, in the UK – 75%, in the USA – 55% of coal are subject to coal preparation. South Africa and Australia, preparing 100% of the exported coal, are the world leaders in coal preparation .
The increase in ash-content of the low-grade fuel by 1% is:
– the loss of power, the reduction of efficiency factor by 0.1-0.15%;
– the need for additional fuel 0.5 g c.t./kWh;
– the additional suspension in production equal to 60 hours per year for repair of the equipment;
-the installation of additional equipment for the fuel preparation and ash and slag removal, the increase in capital expenditures;
– the increase in the electricity consumption for own needs by 0.13%;
– the increase in fuel oil consumption per unit of fuel combusted by 0.6-1.5%.
Numerous studies have conclusively proven the benefit of use of the prepared coal in the energy production industry [7-8].
It was found that the elimination of reduced production of electricity at TPP due to a poor coal could cover all the coal preparation costs, even without so much as the benefit from environmental improvements .
Functional simulation of the production processes
In 1993, the project was developed and the Standard for the functional simulation (IDEF0) was adopted to meet the challenges of this type . Since the beginning of the XXI century the IDEF0 methodology is used as the primary standardization tool in the domestic economy .
The IDEF0 language is standardized in terms of syntax and semantics. The IDEF0 models are three-dimensional, as any two-dimensional IDEF0 diagram can be supplemented by the child functions represented in different layers or levels of the model. The restrictions on the number of child functional layers in the IDEF0 model are absent.
The IDEF0 models are developed and used by the system engineers for simulation and analysis of the complex systems, functional studies of production processes, etc. A number of examples, demonstrating the operational use of IDEF0 are provided both in the domestic and foreign literature [13-15].
In preparing the materials for this article the tools of the free package Ramus Educational , similar to AllFusion Process Modeler 7 (formerly BPwin) were used.
The aim of this work is to prove the correctness of the proposed solution of the problem of coal preparation at TPP prior to combustion and to provide an option of the technological chain of operations performed. The solution to these problems has been obtained on the basis of the methodology of functional simulation IDEF0, which is widely used for different types of the systems .
The traditional scheme of the construction of the “correct” technological process model was used in this work, according to which the transition from the AS-IS model to TO-BE model was performed .
Other methods of systems analysis can be used to solve such problems: the evolutionary algorithms for optimal solutions finding , the multiagent simulation , the parametric optimization , as well as the widespread methods of computational mathematics and mathematical physics .
Criteria for the coal combustion efficiency
The integrated approach allows to select a group of criteria for the coal combustion efficiency, represented in the Table 1. The increase in the coal combustion efficiency can be achieved at the expense of its deep preparation for combustion, including the coal preparation and supplementation to activate the process of combustion and disposal of the emissions.
Table 1: Criteria for the coal combustion efficiency
|No.||Functional group of criteria||Criteria|
|1||Performance and technology||– increase in maneuverability of the power units
– extension of the adjustment range
– reduction of the requirements to the capabilities of the accessories
– reduction of the wear and tear
– extension of the time between the overhauls
|2||Material and technical||– reduction of the reference fuel
– reduction of the need for additional highly reactive fuel
– reduction of excess air ratio
– reduction of the exhaust gases volume
|3||Economical||– reduction of the financial costs on exploitation of TPP
– reduction of the TPP own needs costs
– reduction of the electricity cost
|4||Environmental||– reduction of the amount of harmful emissions
– reduction of the thermal pollution of the atmosphere
– reduction of the soil and groundwater pollution
– change in the physical and chemical properties of the solid and liquid waste
– improvement of the environmental performance of the electricity production process at TPP (gassed space, noise, vibration)
|5||Social||– improvement of the working conditions of the TPP staff
– creation of the preconditions for the development of the side-line productions near TPP
Analysis of the methods of mineral raw materials preparation
The preparation processes are relevant to the mining, metallurgical and chemical sectors of industry [23-24]. All methods of preparation are based on the differences in physical and chemical properties of the substances. The first scientific works on mineral raw materials preparation were related to the extraction of the metal ores. Agricola  in particular, studied the mechanical methods of preparation such as crushing, washing, and the thermal methods – melting in special furnaces. Lomonosov  investigated the separation of the metals from the ores by melting. Modern methods of preparation of the minerals are presented in the Table 2.
Table 2: Methods of mineral raw materials preparation
|No.||Used properties of the minerals and additives to be prepared||Groups of methods of preparation||Methods of preparation||Types of methods of preparation|
|1||Physical||Mechanical||– milling (crushing, grinding)
– dispersion (screening)
– in heavy medium
|Gravity||– gravity separation||– pneumatic
– in heavy medium
– pyrometallurgical (roasting, smelting, distillation)
|Electromagnetic||– electrostatic separation
– magnetic separation
– electromagnetic separation
|Radiometric||– radiometric (for uranium ore)|
|2||Physical and chemical||Surface phenomena, wettability||– flotation|
|Thermal||– thermochemical (melting with the addition of reagents)
– Thermo electrolytic (electrolysis)
|3||Chemical||Selective chemical reactions||– leaching||– hydraulic
|Solubility||– halurgical (solubility difference)
– extraction (transition in a solution)
– method of forming of the poorly soluble compounds (precipitation from solution)
|Other chemical processes||– hydrolysis
– ion exchange method
Analysis of the technological processes
In the late 90-ies of the XX century, most of the coal preparation plants in Russia were closed. This led to a sharp increase in the ash-content of the coal combusted. This situation provides extremely negative impact not only on the performance of the thermal power plants, but also on the environment nearby the power plant. In terms of the macro-economy, it is advisable to perform the coal preparation close by the places of its production with the subsequent sale to the consumers. In the context of the slow rebirth of the centralized coal preparation and sale of the non-prepared coal of variable ash-content to the consumers, it seems appropriate to the authors to include the coal preparation stage in the process of preparation of the air-coal dust mixture (Fig. 1). The proposed innovations are reflected in the diagram TO-BE of the process of coal preparation for combustion (Fig. 2). This diagram also reflects the changes in the process of supply to the boiler, associated with the deep coal preparation for combustion, including, except the preparation, the introduction of additives (activators, catalysts), activating the combustion process.
The context diagram of the TO-BE process of the coal preparation for combustion (Fig. 3), in addition to the described input, output streams and mechanisms for the implementation of the technological operations, shows a list of control and regulatory documents, setting the conditions for the implementation of the technological and logical processes, described in the model.
|Figure 1: Diagram of the process of preparation of the air-coal dust mixture|
|Figure 2: Diagram of the TO-BE process of the coal preparation for combustion|
|Figure 3: Context diagram of the TO-BE process of the coal preparation for combustion|
Coal preparation equipment, available on the special equipment market
The analysis of the literature and the Internet sources allowed to identify the main manufacturers of the coal preparation equipment, available on the market of the Russian Federation (Table 3).
Table 3: Manufacturers of the coal preparation equipment
|No.||Country of origin||Countries and regions-consumers||Trademarks of the equipment||Web-site of the supplier|
|1||China||China Europe, USA, Russia, Ukraine, Brazil, Turkey, South Africa, Kazakhstan, Iran, North Korea, the Philippines, Viet Nam, Indonesia, Mongolia||Batak,
|Equipment from China, www.china-bridge.ru|
|Alliance Oil, alyansoil.com|
|allair®Allmineral, CETCO||Vibrotechtsentr, www.vtcenter.ru|
|4||China||Southeast Asia, Eastern Europe, South America, Middle East, Africa||Liming||Liming LLC, Shanghai Mining Machinery Company, fakmil.com|
|5||South Africa (including under license of Telsmith, American Pulverizer (USA), Mogensen (United Kingdom), IFE (Austria))||South America, Asia, Australia, Russia, CIS countries||Osborn||Ore and rock processing, www.gorniedrobilki.com|
|Russia, CIS countries||Sepair||Gormasheksport, gmexp.ru|
Selection of the coal preparation plant according to the method of T. Saaty
The evaluation of the different variants of the technological equipment was performed based on the hierarchies analysis method of T. Saaty [27-28].
Proceeding from the foregoing list of equipment and its characteristics (Table 3) the list of alternative equipment brands including five positions was completed as follows: FGX (China), SKV (Ukraine), allair®Allmineral (Germany), Osborn (South Africa) and Sepair (Russia).
The criteria for selection of the equipment were determined on the basis of the criteria of the coal combustion efficiency (Table 1): K1 shows the efficiency (the assessment by this criterion involves the proximity of the equipment index to the desired value for the power unit of 300 MW); K2 shows the dimensions (the criterion is focused on the possibility to mount the coal preparation unit near the fuel and transport workshop of TPP); K3 shows the energy consumption (this criterion takes into account the consumption of the electricity by the main and auxiliary machinery of the unit); K4 shows the water consumption (taking into account the need to use water resources); K5 shows the adaptation (this criterion indicates the extent to which the technology used in the unit, complies with the domestic environmental conditions and standards).
The ratings (priorities) for the criteria are set in the range of 1 to 9 where 1 means the equal importance of the criteria, 9 means a very severe superiority of one criterion over the other. The calculation results are presented in the Table 4. The best option of the processing plant is the option number 5 (Sepair, Russia), having a maximum value of a global priority. The option number 2 (SKV, Ukraine) should be noted, which is the second (close) preferred alternative.
Table 4: The results of the evaluation of the alternatives
|The numerical value of the priority vector|
The “Sepair” product line includes the industrial unit with the capacity of 120 t/h of raw coal, while the demand of the coal energy unit of 300 MW is 100 t/h. The coal with the original ash-content of 22-23%, class 14-25 and 25-40 mm is divided by the “SEPAIR” unit in the low-ash coal (ash-content of 8-12%), traded coal (16-18%), middling (35%) enclosing the high-ash solids (tailing, ash-content of 75% or more). The schematic diagram of the “Sepair” unit is shown in the Fig. 4.
|Figure 4: Schematic diagram of the “SEPAIR” pneumatic separator|
Technical and economic effect of the modernization of the facility
The technical and economic analysis of the proposed solutions showed, that for 300 MW power unit at the cost of the coal preparation unit equal to 300 million rubles, the annual fuel consumption equal to 878,400 tons and the fuel price equal to 2000 rub./t:
– the capital investments, including the transportation costs, building and construction works, will amount to 456 million rubles;
– the annual operating costs, including the depreciation deductions and the cost of the annual maintenance, will amount to 41.04 million rubles;
– the annual savings from the reduction of the fuel consumption will be 10,600 tonnes/year, or 21.2 million rubles;
– the reduction of fees for sulfur oxides  emissions will amount to 37.4 million rubles, while the volume of emissions after the event will be reduced by 50%;
– the total annual savings net annual operating costs, related to the coal preparation unit, will be equal to 17.56 million rubles;
– the net income, subject to tax on profits equal to 20%, will amount to more than 14 million rubles;
– the simple payback period, taking into account the net income, depreciation and amortization deductions, will be approximately 12 years from the commissioning of the coal preparation unit “SEPAIR”, but in the case of a modular (simplified) performance of the coal preparation line, by reducing the time and the installation costs, the cost of the coal preparation will be reduced to 25-30 rubles per tonne of raw coal , which will allow to reduce the payback period to 2 years.
Conclusions and recommendations
To solve the problem of high-ash coal combustion efficiency improvement at the thermal power plants it is necessary to develop a new approach to the evaluation of the coal washability as well as the concept of rational use of the steam coal, defining the fundamental improvement in the efficiency of the coal power by the substitution of the mine coal by the prepared coal in the fuel balance of the thermal power plants and the high competitiveness of the prepared coal fuel, commensurate with the other organic energy carriers. These measures will allow to create the technology of environmentally friendly coal-burning fuel and energy complexes. To this end, the authors plan the further development of the simulation models, based on the agent approach to the thermal power plants for the rapid assessment of the effectiveness of the solutions, similar to the solutions, proposed in this work, for the specific power plants, and, possibly, the regions.
The work was financially supported by the Ministry of Education and Science of the Russian Federation in the framework of the implementation of the FTP “Research and development on the priority development fields of the scientific and technological complex of Russia for 2014-2020” (Agreement No 14.574.21.0018 on “Development of the method for the intensification of the low-reactive coal gasification process in an upward jet-vortex of the oxidant.” Unique identifier PNI (of the Project) RFMEFI57414X0018).
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