000 | 03701nlm1a2200457 4500 | ||
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001 | 649445 | ||
005 | 20231030040911.0 | ||
035 | _a(RuTPU)RU\TPU\network\14607 | ||
035 | _aRU\TPU\network\9679 | ||
090 | _a649445 | ||
100 | _a20160713a2016 k y0engy50 ba | ||
101 | 0 | _aeng | |
135 | _adrcn ---uucaa | ||
181 | 0 | _ai | |
182 | 0 | _ab | |
200 | 1 |
_aStudy of ignition, combustion, and production of harmful substances upon burning solid organic fuel at a test bench with a vortex chamber _fA. P. Burdukov [et al.] |
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203 |
_aText _celectronic |
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300 | _aTitle screen | ||
320 | _a[References: p. 67 (4 tit.)] | ||
330 | _aResults of investigation of furnace processes upon burning of pulverized fuel at a test bench with a power of 5 MW are presented. The test bench consists of two stages with tangential air and pulverized coal feed, and it is equipped by a vibrocentrifugal mill and a disintegrator. Such milling devices have an intensive mechanical impact on solid organic fuel, which, in a number of cases, increases the reactivity of ground material. The processes of ignition and stable combustion of a mixture of gas coal and sludge (wastes of concentration plant), as well as Ekibastus coal, ground in the disintegrator, were studied at the test bench. The results of experimental burning demonstrated that preliminary fuel grinding in the disintegrator provides autothermal combustion mode even for hardly inflammable organic fuels. Experimental combustion of biomass, wheat straw with different lignin content (18, 30, 60%) after grinding in the disintegrator, was performed at the test bench in order to determine the possibility of supporting stable autothermal burning. Stable biofuel combustion mode without lighting by highly reactive fuel was achieved in the experiments. The influence of the additive GTS-Powder (L.O.M. Leaders Co., Ltd., Republic of Korea) in the solid and liquid state on reducing sulfur oxide production upon burning Mugun coal was studied. The results of experimental combustion testify that, for an additive concentration from 1 to 15% of the total mass of the burned mixture, the maximum SO2 concentration reduction in ejected gases was not more than 18% with respect to the amount for the case of burning pure coal. | ||
333 | _aРежим доступа: по договору с организацией-держателем ресурса | ||
461 | _tThermal Engineering | ||
463 |
_tVol. 63, iss. 1 _v[P. 61-67] _d2016 |
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610 | 1 | _aэлектронный ресурс | |
610 | 1 | _aтруды учёных ТПУ | |
610 | 1 | _aзажигание | |
610 | 1 | _aкатализаторы | |
610 | 1 | _aоксиды серы | |
610 | 1 | _aбиомассы | |
610 | 1 | _aразрыхлители | |
610 | 1 | _aпылевидное топливо | |
701 | 1 |
_aBurdukov _bA. P. |
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701 | 1 |
_aChernetskiy _bM. Yu. |
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701 | 1 |
_aDekterev _bA. A. |
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701 | 1 |
_aAnufriev _bI. S. |
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701 | 1 |
_aStrizhak _bP. A. _cSpecialist in the field of heat power energy _cDoctor of Physical and Mathematical Sciences (DSc), Professor of Tomsk Polytechnic University (TPU) _f1985- _gPavel Alexandrovich _2stltpush _3(RuTPU)RU\TPU\pers\30871 |
|
701 | 1 |
_aGreben’kov _bP. Yu. |
|
712 | 0 | 2 |
_aНациональный исследовательский Томский политехнический университет (ТПУ) _bЭнергетический институт (ЭНИН) _bКафедра теоретической и промышленной теплотехники (ТПТ) _h117 _2stltpush _3(RuTPU)RU\TPU\col\18679 |
801 | 2 |
_aRU _b63413507 _c20160713 _gRCR |
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856 | 4 | _uhttp://dx.doi.org/10.1134/S0040601515120046 | |
942 | _cCF |