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Boreskov Institute of Catalysis of the Siberian Branch of Russian ...

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OP-V-15An effect <strong>of</strong> preliminary RH carbonization conditions and o<strong>the</strong>r conditions <strong>of</strong> <strong>the</strong> processes<strong>of</strong> <strong>the</strong> alkali activation and <strong>the</strong> high-temperature leaching <strong>of</strong> SiO 2 by <strong>the</strong> mixture <strong>of</strong>K 2 CO 3 /Na 2 CO 3 on properties <strong>of</strong> <strong>the</strong> preparing materials was investigated. It was showed, that<strong>the</strong> carrying out <strong>the</strong> carbonization in fluidized catalyst bed (T = 450–600 °C, contact time τ ~ 1sec, molar ratio <strong>of</strong> air oxygen to carbon <strong>of</strong> RH α ∼ 2, catalyst <strong>of</strong> deep oxidation CuO + MgO +Cr 2 O 3 /γ-Al 2 O 3 with granule’s size 2–3 mm) <strong>of</strong> leads to preparation <strong>of</strong> carbon-silica compositeswith better properties for preparation <strong>of</strong> <strong>the</strong> final carbons, than in case <strong>of</strong> pyrolysis.In Table 1, <strong>the</strong> results <strong>of</strong> an investigation <strong>of</strong> an effect <strong>of</strong> activation temperature on textureand adsorptive properties in relation to hydrogen and methane <strong>of</strong> <strong>the</strong> microporous carbonsprepared from RH, carbonized in fluidized catalyst bed at 500 °C are listed.Table 1. Activation temperature effect on texture and adsorptive properties <strong>of</strong> microporouscarbon samples obtained at different temperatures by KOH activation.A BET ,m 2 g –1V Σ /V μ , mlg –1Vol. microporequota, %H 2 adsorptive capacity,w. % (50 bar, 77 K)700 3170 1.77/1.45 81.9 4.7 28750 3450 2.01/1.68 83.6 5.7 27800 3360 2.18/1.87 92.3 6.3 33850 3170 2.26/1.74 77.0 5.8 34900 3210 2.97/1.48 49.8 6.2 41Activationtemperature, °CCH 4 adsorptive capacity,w. % (60 bar, 273 K)The analogies <strong>of</strong> <strong>the</strong> materials – microporous carbons, such as Maxsorb (Kansai Coke andChemical Co Ltd., Japan) are produced from petroleum coke and pitch also by KOHactivation at 700–800 °C but through a preliminary treatment <strong>of</strong> <strong>the</strong> precursors byconcentrated nitric acid that leads to mordant and toxic wastes. In addition, <strong>the</strong>se materialspossess lower texture characteristics (A BET about 2700 m 2 g –1 , V μ about 1.2 ml g –1 ) [4]. Acomparison <strong>of</strong> <strong>the</strong> technical conditions leads to a resume that <strong>the</strong> proposing method is cheaperand environmentally more appropriate.In Table 2 <strong>the</strong> data on an effect <strong>of</strong> temperature on mesoporous carbons properties areshowed. The carbons were prepared by high-temperature leaching <strong>of</strong> SiO 2 from RH,carbonized in <strong>the</strong> fluidized catalyst bed reactor, by pyrolysis in inert atmosphere and fromnon-carbonized RH.Table 2. Effect <strong>of</strong> <strong>the</strong> leaching temperature on texture properties <strong>of</strong> mesoporous carbonsprepared from RH by high-temperature leaching with equimolar Na 2 CO 3 /K 2 CO 3 mixturePretreatmentconditionsT, °CVol.A BET ,m 2 g –1 V Σ /V µ , ml g –1 mesoporequota, %Deep <strong>of</strong> graphitization,% (by XRD)Ash content,%FCB 1) , 500 °C 750 1190 1.11/0.20 82.0 0.0 1.7FCB, 500 °C 800 1485 1.36/0.29 78.7 0.0 2.4FCB, 500 °C 850 1447 1.24/0.31 75.0 0.0 4.5FCB, 500 °C 900 1581 1.44/0.31 78.5 0.0 2.0FCB, 500 °C 950 776 0.88/0.21 76.1 39.5 1.8FCB, 500 °C 1000 652 0.84/0.13 84.5 46.5 2.3Pyrolysis, 400 °C 900 1479 1.17/0.40 65.82) - 4.1- 3) 900 1350 1.00/0.49 51.0 - 4.51) – FCB – fluidized catalyst bed; 2) – not investigated; 3) – raw RH was used197

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