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CARBONACEOUS ROCKS OF DNIEPROVSKY BROWN COAL BASIN AS A RAW MATERIAL FOR POWER ENERGETIC AND CHEMICAL INDUSTRIES.

V.I. Saranchuk, G.P. Matsenko, V.I. Tamko, I.I. Shwets


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Источник: Proceedincs of the IV European coal conference, 26-28 September 2000, Ustron, Poland, Polish Geological institute special papers, Warszawa 2002. – Vol. 7, P. 225-227.



      Carbonaceous rocks are high ash carbonaceous formations that mostly are deposited in the roof of the brown coal bed. Its quantity achieved 50 % of the mining coal. They are occurring in the dumps while coal being mined.
      Dnieprovsky brown coal basin situated in the central part of Ukraine, unifies more than 150 brown coal deposits, area of from 200 up to 400 km2, located mostly by the right coast of the Dnieper river. About 55 deposits are of an industrial value mostly in Alexandriysky brown coal region of Dniepropetrovsk and Kirovograd oblasts. The coal reserves explored consist of 2.4 billion tons.
      The industrial coal carrying is related to precipitation of Buchaksky layer of paleogene (medium eocene). Coal-carrying precipitation of Buchack layer by lythological characteristics are divided into three main stratae (horizons): under-coal, coal and per carbonic ones.
      Under-coal layer is composed of medium and large-size grain grey sands, that transfer in its upper part into fine dark-brown carbonaceous, clay lenses, kaolins, seldom fine coal interlayers. A maximum capacity of a horizon is 25 m, predominating one is 6-8 m.
      The coal rock mass is a unique stock formed more or less in the same time that represents one layer of a simple or complicated construction, less often 2-3 layers separated by carbonaceous sands, carbonaceous clays, sand interlayers. The capacity and composition of coal deposit are not stable, being sharply changed with a coal transition into carbonaceous rocks, high ash coals (mainly in upper part of a deposit).
      A percarbonic rock mass is composed of carbonaceous clays, carbonaceous sands with clay interlayers, sands, lenses and coal interlayers. A total capacity of Buchack precipitation do not exceed 40-45 m, often – 10-15 m [1].
      Carbonaceous clays and sands are related to the category of mine rocks only because the ash content in it is more than 40 %. If this conditionally boundary would be accepted as equal to 50 %, then coal resources would increase 1.5-2 times and the thickness of stripping would decrease 2-3 times.
      Our investigations revealed that carbonaceous rocks are similar by their composition and properties to brown coal, with the ash content from 40 to 60 %, the same composition of elements of organic matter, yield of bitumen and humic acids.
      Preliminary investigations reveled that carbonaceous rocks when utilized in complex may be used as an energy-producing and chemical resource, the base of good carbon adsorbents.

EXPERIMENTAL


      For the processing of carbonaceous clays (CC) the pyrolysis was used [2]. Both source CC and CC preliminary processed by 1M solution of NaOH. CC were decomposed by heat at a temperature of 600-900 0C in the reactor without pressure. The resultant steam-gas mixtures were separated into liquid products and gas. Sorbents from CC were received by the activation fixed residues (carbonizates) of CC pyrolysis by water vapor. Sorption volume of the resultant sorbents was determined from methylene blue and phenol. Specific surface of sorbents was determined by BET method. This paper shows results of the processing of CC on the example of CC from Verbolozovskiy stripping of Alexandriyskiy deposit.

RESULTS AND DISCUSSIONS


      Table 1 contains outlet of pyrolysis products of CC from Verbolozoskiy stripping at various temperatures. The yield of liquid products from CC increases up to the temperature of 700 0C. At higher pyrolysis temperatures only gases are produced from CC processed by NaOH is 1.4 times higher than from source CC, gas outlet being by 5-15 % higher. Thus, from 1 t of organic masse CC contained in 1.7 t of dry CC 80-120 kg of liquid products, 320-610 kg or 250-470 m3 of gas and 1000-1250 kg of carbonizate (source for adsorbents) may be received.

Table 1. Yield of CC pyrolysis products
Pyrolysis temperature,°С Yield of pyrolysis products OM conversion degree, %
Liquid, % of OM Gas, % of OM Carbonizate, % of ОМ Carbonizate , % of dry CC
Parent CC
600 8,0 32 60 73 40
700 9,0 44 47 67 53
800 9,0 49 42 65 58
900 9,0 59 32 62 68
CC treated by 1М solution of NaOH
600 11,0 37 52 72 48
700 12,0 45 43 70 57
800 12,0 51 37 68 63
900 12,0 61 27 65 73


      The use of carbonizates in the power industry is not expedient because they contain high (58-70 %) content of ash. Thus the expediency of CC processing depends on the opportunities to receive quality adsorbents from them. Table 2 demonstrates data on the outlet and properties of adsorbents received from CC carbonizates.
      Specific surface of adsorbents from CC is lower than from adsorbents received from brown coal. Sorption capacitance of adsorbents from CC equals to adsorbents received in similar conditions from brown coal. Adsorbents from CC treated by NaOH possess lower specific surface than adsorbents from initial CC. But their use is expedient to receive granulated adsorbents from finely divided (fractions<0.5 mm). The yield of sorbents from CC is 1.5-1.6 times higher then from brown coals. Adsorbents from CC meet requirements to clarifying adsorbents and can be recommended for the removal of harmful impurities from sewage and air.
      

Table 2. Adsorbents from CC of Verbolozovskiy stripping
Name Receiving conditions Yield, % of dry CC Ash content, % Specific surface, m2/g Adsorption capacitance
t, °С Activation time, min of methylene blue, mg/g of phenol, %
Parent CC 40 3,0 54
Carbonizate from parent CC 900 63 63 120 52 56
Adsorbent from parent CC 925 30 59 67 205 80 85
Carbonizate from CC treated by NaOH 900 58 73 61 58 50
Adsorbent from CC treated by NaOH 925 30 54 79 110 78 72
Adsorbent from brown coal 925 30 38 26 515 77 80

CONCLUSIONS


      While analyzing results of these investigations it can be noted that the use of CC as a raw material for the power and chemical industries is possible under their complex processing

Literature


      1. Dneprovskiy brown coal basin/ A.Y. Radzivill and others – K.: Naukova Dumka, 1987. – 328 p.
      2. V.I. Saranchuk, V.A. Tamko// Khimia Tverdogo Topliva. 1986 №6 p.55-60.