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    • 3. 发明授权
    • Method of producing dispersions and carrying out of chemical reactions in the disperse phase
    • 在分散相中产生分散体并进行化学反应的方法
    • US06321998B1
    • 2001-11-27
    • US09068264
    • 1998-05-05
    • Klaus SchubertWilhelm BierGerd LinderErhard HerrmannBernd KoglinThomas Menzel
    • Klaus SchubertWilhelm BierGerd LinderErhard HerrmannBernd KoglinThomas Menzel
    • A62C502
    • B01F5/0256B01F5/0644B01F13/00B01F13/0059B01J19/0093B01J2219/00783B01J2219/00889Y10S366/03
    • In the process for the continuous dispersion of at least one fluid A constituting the disperse phase and at least one continuous phase constituting the enclosing phase of a fluid B, at least one fluid stream A and at least one fluid stream B are fed into a dispersion apparatus and come into contact therein in a dispersion chamber. To this end, a microstructure dispersion apparatus (1a, 1b, 3a, 3b) is used in which the fluid streams A, B are broken up into spatially separate, flowing fluid filaments by a system of microchannels (1a, 1b) associated therewith, which filaments are discharged into the dispersion chamber (4) at identical flow velocities for the particular fluid in such a manner that on discharge into the dispersion chamber (4) a fluid jet (6a) of the disperse phase is in each case immediately adjacent to a fluid jet (6b) of the continuous phase and in each case a fluid jet (6a) of the disperse phase is enclosed as it is broken up into particles in the adjacent fluid jets (6b) of the continuous phase.
    • 在构成分散相的至少一种流体A和构成流体B的封闭相的至少一个连续相的连续分散的过程中,将至少一种流体流A和至少一种流体流B进料到分散体 装置并在分散室中与其接触。 为此,使用通过与其相关联的微通道(1a,1b)的系统将流体流A,B分解成空间分离的流动细丝的微结构分散装置(1a,1b,3a,3b) 以特定流体的相同流速将这些细丝排出到分散室(4)中,使得在排放到分散室(4)中时,分散相的流体射流(6a)在每种情况下都紧邻于 在连续相的流体射流(6b)中,并且在每种情况下,分散相的流体射流(6a)被包围,因为其在连续相的相邻流体射流(6b)中被分解成颗粒。
    • 8. 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。