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Nitrogen balances in recovery boilers

机译:回收锅炉中的氮气平衡

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Nitrogen balances can vary a lot between different mills and recovery boilers.This presentation is based on nitrogen balance measurements for 17 boilers.They show that in modern new boilers the N conversion factor from black liquor N into nitrogen in NO_x is typically in the range of 20-30%.When the boiler design has been done specially for low-NO_x emissions,the range is 15-20%.The nitrogen split can be with low-NO_x design for instance 15% into NO_x,10% into smelt and 75% into N2 in flue gases.Low NO_x emission does not correlate with high concentration of N in out flowing smelt.On the other hand,N concentration in smelt can represent over 40% of the incoming N in black liquor.The emission figures correlate with excess air,temperatures,staging,and in some cases with carry-over.The balance figures of the presentation vary with the firing system,with the loadings,with liquor firing properties including dry solids,with the operation parameters etc.The missing data for reliable numerical modeling,without experience related parameters,are in pyrolysis and lower furnace oxidation processes,including deep temperature,concentrations and velocity gradients.The effect of weak and strong odorous gases into NO_x emission,depend on system design.With right design,the N input via NH3 in the odorous gases does not effect the NO_x emissions of recovery boilers.The important,practical issue is that NO_x emission and other emissions have cross effects,data for BAT has to be from the same recovery boiler in this respect.Lower NO_x emission may generate S02 emission,and the operation mode,which results into low NO_x emission may affect on the melting behavior of carry-over.Lower melting temperature can induce fouling and corrosion in the superheater;more sootblowing steam is needed and the generation capability of greenhouse gas free power is reduced.Naturally the corrosion issue can be compensated with more expensive materials.The other important practical issue is that generally boiler loading has effect on NO_x emission via temperatures.If the permit is for the today's firing capacity,the capacity increase will result into higher specific NO_x releases,and into higher emissions per ADt pulp.
机译:在不同的轧机和回收锅炉之间的氮气平衡可以变化很大。此介绍是基于17个锅炉的氮气平衡测量。他们表明,在现代新的锅炉中,NO_X中的黑液N转化为氮气的转换因子通常在范围内20-30%。当锅炉设计专门用于低NO_X排放时,该范围为15-20%。氮气分裂可以用低NO_X设计,例如15%进入NO_X,10%进入熔炼和75烟气中的N2中的%.Low NO_X排放与高浓度的N型流动浓度不相关。另一方面,熔炼中的N浓度可以代表黑液中的40%超过40%。排放数据与过量的空气,温度,分期,以及在某些情况下随续集的情况。演示的平衡数据随着烧制系统而随着燃烧系统,液体烧制特性,包括干固体,操作参数等缺失数据可靠的数值建模,没有经验相关参数,是在热解和下炉氧化过程中,包括深温,浓度和速度梯度。弱和强烈的有气气体进入NO_X排放,依赖于系统设计。与正确的设计,N个输入NH3在有吸气气体中没有影响回收锅炉的NO_X排放。重要的实际问题是NO_X排放和其他排放具有交叉效果,BAT的数据必须在这方面的来自相同的回收锅炉。呼吸器发射可能产生S02发射,并且导致低NO_X发射的操作模式可能会影响随身携带的熔化行为.Lower熔化温度可以在过热器中诱导污垢和腐蚀;需要更多的扫描蒸汽和温室气体的产生能力。温室气体自由电量减少。腐蚀问题可以用更昂贵的材料得到补偿。其他重要的实际问题一般是博ILER负载通过温度对NO_X发射产生影响。如果许可证用于当今的射击能力,则容量增加将导致更高的特定NO_X释放,并进入每个ADT纸浆的更高排放。

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