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    • 5. 发明授权
    • Process and apparatus for removing dust, sulfur compounds and nitrogen
oxides from combustion exhaust gases
    • 从燃烧排气中去除灰尘,硫化物和氮氧化物的方法和装置
    • US5219543A
    • 1993-06-15
    • US803185
    • 1991-12-05
    • Werner WeisweilerErhard HerrmannWolfgang FennemannHarald SauerBernd Thone
    • Werner WeisweilerErhard HerrmannWolfgang FennemannHarald SauerBernd Thone
    • B01D53/60
    • B01D53/60
    • The process of removing dust, sulfur compounds and nitrogen oxides from combustion exhaust gases, comprising mixing a combustion exhaust gas with ammonia; feeding Ca(OH).sub.2 and FeSO.sub.4 to a fluidized bed reactor containing mixed solids including fly ash, iron sulfates and calcium compounds, especially Ca(OH).sub.2, CaCO.sub.3, CaO, CaSO.sub.4 and CaSO.sub.3 ; supplying an ammonia-containing exhaust gas mixture to the fluidized bed reactor as a fluidizing gas; operating the fluidized bed reactor at a temperature between 300.degree. and 450.degree. C. to form a reacted exhaust gas; supplying the reacted exhaust gas to a multistage electrostatic precipitator having a first stage and additional stages; recycling solids collected in the first stage to the fluidized bed reactor; and recycling one portion of additional solids collected in the additional stages to the fluidized bed reactor and discharging another portion of the additional solids.
    • 从燃烧废气中除去灰尘,硫化合物和氮氧化物的过程,包括将燃烧废气与氨混合; 将Ca(OH)2和FeSO 4加入到包含飞灰,硫酸铁和钙化合物,特别是Ca(OH)2,CaCO 3,CaO,CaSO 4和CaSO 3的混合固体的流化床反应器中; 将作为流化气体的含氨废气混合物供给流化床反应器; 在300-450℃的温度下操作流化床反应器以形成反应废气; 将反应的废气供应到具有第一级和附加级的多级静电除尘器; 将在第一阶段收集的固体回收到流化床反应器; 并将在附加阶段收集的一部分附加固体回收到流化床反应器中并排出另外部分的附加固体。
    • 9. 发明授权
    • Process and device for cleaning combustion flue gases
    • 用于清洁燃烧烟气的工艺和装置
    • US07776298B2
    • 2010-08-17
    • US10190644
    • 2002-07-08
    • Hansjörg HerdenBarbara RothRobert MerglerBerthold StegemannHarald Sauer
    • Hansjörg HerdenBarbara RothRobert MerglerBerthold StegemannHarald Sauer
    • B01D53/52
    • B01D53/64B01D53/12B01D53/508B01D53/68B01D2253/102B01D2253/108B01D2257/2045B01D2257/2047B01D2257/206B01D2257/302B01D2257/60B01D2257/602F23J15/006F23J2219/30F23J2219/50
    • The invention relates to a process and a device for the removal of dust, HF, HCl, SO2, SO3, heavy metals, heavy-metal compounds, polyhalogenated hydrocarbons and polycyclic hydrocarbons from combustion flue gases by treating the pollutant-containing combustion flue gases with a sorbent in a circulating fluidized bed. The process is characterized in that the sorbent used is a mixture of Ca(OH)2, at least one naturally occurring zeolite and a carbon-containing substance, in that the treatment of the pollutant-containing combustion flue gases with the sorbent is carried out at from 120 to 180° C. in the presence of water/steam, in that the reactor (3) of the circulating fluidized bed is operated at a gas velocity of from 2 to 10 m/s, a mean residence time of the solids particles in the case of a single pass of from 1 to 10 seconds, and a solids circulation rate of from 10 to 100, where the gas/solid suspension present in the reactor (3) has a mean suspension density of from 1 to 10 kg of solid/Nm3 of flue gas, and in that the removal of the loaded sorbent is carried out by filtration.
    • 本发明涉及一种从燃烧烟气中去除灰尘,HF,HCl,SO2,SO3,重金属,重金属化合物,多卤代烃和多环烃的方法和装置,通过处理含污染物的燃烧烟道气 循环流化床中的吸附剂。 该方法的特征在于所用的吸附剂是Ca(OH)2,至少一种天然存在的沸石和含碳物质的混合物,因为用吸附剂处理含污染物的燃烧烟道气 在水/蒸汽存在下为120-180℃,循环流化床的反应器(3)以2至10m / s的气体速度运行,固体的平均停留时间 在单次通过的情况下为1至10秒的颗粒,以及10至100的固体循环速率,其中存在于反应器(3)中的气体/固体悬浮液具有1至10kg的平均悬浮密度 的固体/ Nm 3的烟道气,并且通过过滤进行负载的吸附剂的去除。