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    • 2. 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。
    • 3. 发明授权
    • Process for manufacturing ceramic, diffusion-limiting layers and use of
these layers
    • 制造陶瓷,扩散限制层和使用这些层的方法
    • US6086948A
    • 2000-07-11
    • US313941
    • 1999-05-19
    • Barbara RothVolker BruserUlrich Guth
    • Barbara RothVolker BruserUlrich Guth
    • C04B41/89C04B35/00C04B41/45C04B41/81G01N27/407B05D1/12B05D1/32B05D5/12
    • C04B41/009C04B41/4582C04B41/81G01N27/407G01N27/4071
    • Porous, ceramic layers, which also have a diffusion-limiting action, are as a rule manufactured by selectively adding pore formers to the ceramic sinter material. The porosity of the layer created in this way lies in the micrometer range. The known processes for manufacturing layers of this type are intended for application to planar substrates. Suitability for spherical surfaces and a porosity of the layer in the nanometer range is provided herein by an oxide ceramic powder having a BET specific surface area in the range of about 5 to 50 m.sup.2 /g and having a mean primary particle size of about 20 to 450 nm. The powder is first pretreated at a temperature of about 800.degree. C. to 1150.degree. C. and then mixed with untreated, oxide ceramic powder. The mixture is then applied to a high temperature-stable base, and burned-in (fired) at a temperatures of about 1000.degree. C. to 1350.degree. C. Optionally, instead of the thermally pretreated oxide ceramic powder, a recrystallized glass powder can be used. The firing temperature range in this case, however, is about 850.degree. C. to 1000.degree. C.
    • 通常通过向陶瓷烧结材料中选择性地添加成孔剂制造的多孔陶瓷层也具有扩散限制作用。 以这种方式产生的层的孔隙率在微米范围内。 用于制造这种类型的层的已知方法旨在用于平面基板。 通过氧化物陶瓷粉末提供球形表面的适合性和纳米范围内的层的孔隙率,所述氧化物陶瓷粉末的BET比表面积为约5至50m 2 / g,平均初级粒度为约20至 450nm。 首先将粉末在约800℃至1150℃的温度下预处理,然后与未处理的氧化物陶瓷粉末混合。 然后将混合物施加到高温稳定的碱,并在约1000℃至1350℃的温度下燃烧(烧制)。可选地,代替热预处理的氧化物陶瓷粉末,再结晶的玻璃粉末可以 使用。 然而,这种情况下的烧成温度范围为约850℃〜1000℃