2021
DOI: 10.1134/s004060152106001x
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Development of SNCR Technology and Prospects of Its Application

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Cited by 9 publications
(5 citation statements)
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“…The main disadvantages of SNCR are the ammonia slip, that there should be little or no hydrocarbons or CO present, and the narrow temperature range (900−1050 °C when using urea) for its maximum efficiency. 9 In SCR, the ammonia is chemisorbed on a catalyst and reacts with NO or NO 2 from the gas phase, enabling operation at lower temperatures, usually between 250 and 400 °C, 11 but the SCR technique is limited due to poisoning of the catalyst, particularly, in flue gases containing high amounts of fly ash or dust.…”
Section: Introductionmentioning
confidence: 99%
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“…The main disadvantages of SNCR are the ammonia slip, that there should be little or no hydrocarbons or CO present, and the narrow temperature range (900−1050 °C when using urea) for its maximum efficiency. 9 In SCR, the ammonia is chemisorbed on a catalyst and reacts with NO or NO 2 from the gas phase, enabling operation at lower temperatures, usually between 250 and 400 °C, 11 but the SCR technique is limited due to poisoning of the catalyst, particularly, in flue gases containing high amounts of fly ash or dust.…”
Section: Introductionmentioning
confidence: 99%
“…NO x emissions resulting from thermal conversion of solid and liquid fuels, and also from other industrial processes, continue to be a major challenge for environmental reasons and due to increasingly strict emission limits. In the last 50 years, numerous studies investigated the formation and chemistry of NO x emissions experimentally, computationally, and at an industrial scale. NO x emissions can be reduced by selective noncatalytic reduction (SNCR) and selective catalytic reduction (SCR). , In the SNCR process, NO and NO 2 are reduced to N 2 by injecting ammonia (NH 3 ) or urea (CO­(NH 2 ) 2 ) in the presence of oxygen. The main disadvantages of SNCR are the ammonia slip, that there should be little or no hydrocarbons or CO present, and the narrow temperature range (900–1050 °C when using urea) for its maximum efficiency .…”
Section: Introductionmentioning
confidence: 99%
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“…Since Lyon invented the SNCR technology for NO removal in 1975, this technology, which uses reducing agents without catalysts to reduce nitrogen oxides at specific flue gas temperatures, has been a highly costeffective approach. The advantages of applying SNCR in coal powder boilers are mature technology, small system footprint, low investment cost, short construction period, and small impact on boiler operation [3] , In garbage incinerators, power generation efficiency can also be improved [4] . The disadvantage is that the denitrification efficiency decreases with the increase of furnace size, and the efficiency is not high in practical applications [5] .…”
Section: Introductionmentioning
confidence: 99%
“…However, due to the low volatility and poor reactivity of anthracite, it inevitably suffers from the difficulties of ignition and burn-out [ 2 ], resulting in severe environmental problems such as photochemical smog, acid rain, forest deterioration, and ozone depletion [ 3 ]. Owing to the strict standards for NOx emissions in China (decreased below 50 mg/m 3 at 6% O 2 ) [ 4 ], numerous researchers have made great efforts to lower NOx emissions, including through selective catalytic reduction (SCR) [ 5 ], selective non-catalytic reduction (SNCR) [ 6 ], low-NOx burners [ 7 ], and air/fuel staged combustion technology [ 8 ]. However, these methods have inevitably exhibited limitations such as catalyst pollution, ammonia leaking, and high operational cost.…”
Section: Introductionmentioning
confidence: 99%