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    • 22. 发明授权
    • Cyclone separator
    • 旋风分离器
    • US07323023B2
    • 2008-01-29
    • US11009889
    • 2004-12-10
    • Volker MicheleHeiko HeroldGuenther Sanchen
    • Volker MicheleHeiko HeroldGuenther Sanchen
    • B01D45/12B01D50/00
    • B04C9/00B04C3/04B04C3/06B04C2009/004B04C2009/005B23Q11/0046
    • A cyclone separator (14) for use in a suction apparatus (4) of a hand-held power tool (2) includes a dirty air inlet (12), a suction ventilator (38) for aspirating, through a suction opening (8) which is connected with the dirty air inlet (12), abrasion particle-carrying suction air, a pure air outlet for letting out purified air, a vortex chamber (16) arranged between the dirty air inlet (12) and the pure air outlet, with the dirty air inlet (12) opening substantially tangentially into the vortex chamber (16) for generating a swirling stream in a direction toward the pure air extraction element (24), a collection chamber (36), and particle outlet having at least two particle outlet openings and connecting the vortex chamber with a collection chamber (36), with the dirty air inlet opening into the vortex chamber between the two particle outlet openings.
    • 用于手持式电动工具(2)的抽吸装置(4)的旋风分离器(14)包括脏空气入口(12),用于通过吸入口(8)吸入的抽吸通风机(38) 与脏空气入口(12)连接,具有吸附颗粒的吸入空气,用于排出净化空气的净空气出口,设置在脏空气入口(12)和净空气出口之间的涡流室(16) 其中脏空气入口(12)基本上相切地打开到涡流室(16)中,用于沿朝向纯空气抽取元件(24)的方向产生旋流,收集室(36)和具有至少两个 颗粒出口开口并将涡流室与收集室(36)连接,脏空气入口通入两个颗粒出口之间的涡流室。
    • 23. 发明授权
    • Process for the production of dinitrotoluene
    • 生产二硝基甲苯的方法
    • US07041858B1
    • 2006-05-09
    • US11054012
    • 2005-02-09
    • Juergen MuennigBernd PennemannDietmar WastianVolker MicheleJesse CaravaggioJohn F. Gisch, Jr.
    • Juergen MuennigBernd PennemannDietmar WastianVolker MicheleJesse CaravaggioJohn F. Gisch, Jr.
    • C07C205/00
    • C07C201/08C07C205/06
    • The present invention is directed to a process for the isothermal nitration of aromatic organic compounds, wherein an aromatic organic compound is brought into contact and reacted with a mixture of sulfuric acid and nitric acid. The mixture of sulfuric acid and nitric acid, and the aromatic organic compound are brought into contact with each other through a mixing nozzle which comprises a substantially cylindrical tubular reactor and an annular gap which surrounds the tubular reactor. The aromatic organic compound flows through the tubular reactor, and the mixture of sulfuric acid and nitric acid flows through the annular gap, and they are mixed together upon emerging from the tubular reactor and the annular gap, wherein the ratio of the average rates of flow of the aromatic organic compound in the tubular reactor, and of the mixture of sulphuric acid and nitric acid in the annular gap ranges from 0.5:1 to 10:1.
    • 本发明涉及芳族有机化合物的等温硝化方法,其中使芳族有机化合物与硫酸和硝酸的混合物接触并反应。 硫酸和硝酸的混合物和芳香族有机化合物通过混合喷嘴相互接触,所述混合喷嘴包括基本上圆柱形的管式反应器和围绕管状反应器的环形间隙。 芳族有机化合物流过管状反应器,硫酸和硝酸的混合物流过环形间隙,并且在从管式反应器和环形间隙出现时将它们混合在一起,其中平均流速 的管状反应器中的芳族有机化合物,以及环状间隙中的硫酸和硝酸的混合物的范围为0.5:1至10:1。
    • 24. 发明申请
    • Cyclone separator
    • 旋风分离器
    • US20050150199A1
    • 2005-07-14
    • US11009889
    • 2004-12-10
    • Volker MicheleHeiko HeroldGuenther Sanchen
    • Volker MicheleHeiko HeroldGuenther Sanchen
    • B01D50/00B04C3/04B04C3/06B04C5/12B04C5/185B04C5/187B04C9/00B23Q11/00
    • B04C9/00B04C3/04B04C3/06B04C2009/004B04C2009/005B23Q11/0046
    • A cyclone separator (14) for use in a suction apparatus (4) of a hand-held power tool (2) includes a dirty air inlet (12), a suction ventilator (38) for aspirating, through a suction opening (8) which is connected with the dirty air inlet (12), abrasion particle-carrying suction air, a pure air outlet for letting out purified air, a vortex chamber (16) arranged between the dirty air inlet (12) and the pure air outlet, with the dirty air inlet (12) opening substantially tangentially into the vortex chamber (16) for generating a swirling stream in a direction toward the pure air extraction element (24), a collection chamber (36), and particle outlet having at least two particle outlet openings and connecting the vortex chamber with a collection chamber (36), with the dirty air inlet opening into the vortex chamber between the two particle outlet openings.
    • 用于手持式电动工具(2)的抽吸装置(4)的旋风分离器(14)包括脏空气入口(12),用于通过吸入口(8)吸入的抽吸通风机(38) 与脏空气入口(12)连接,具有吸附颗粒的吸入空气,用于排出净化空气的净空气出口,设置在脏空气入口(12)和净空气出口之间的涡流室(16) 其中脏空气入口(12)基本上相切地打开到涡流室(16)中,用于沿朝向纯空气抽取元件(24)的方向产生旋流,收集室(36)和具有至少两个 颗粒出口开口并将涡流室与收集室(36)连接,脏空气入口通入两个颗粒出口之间的涡流室。
    • 25. 发明授权
    • Process for the preparation of isocyanates in the gas phase
    • 在气相中制备异氰酸酯的方法
    • US09024057B2
    • 2015-05-05
    • US12632117
    • 2009-12-07
    • Klaus BiskupRainer BrunsWolfgang LorenzFritz PohlFriedhelm SteffensVolker Michele
    • Klaus BiskupRainer BrunsWolfgang LorenzFritz PohlFriedhelm SteffensVolker Michele
    • C07C263/00C07C263/10
    • C07C263/10C07C265/14
    • Aromatic isocyanates are produced by reacting one or more aromatic primary amines with phosgene in the gas phase. The phosgene and primary aromatic amine(s) are reacted at a temperature above the boiling temperature of the amine(s) in a reactor having a reaction space which is essentially rotationally symmetric to the direction of flow. The flow fate, averaged over the cross-section, of the reaction mixture along the axis of the essentially rotationally symmetric reaction space in the section of the reaction space in which the conversion of the amine groups into isocyanate groups is between 4 and 80% is not more than 8 m/sec. The flow rate averaged over the cross-section of the reaction mixture along the axis of the essentially rotationally symmetric reaction space in the section of the reaction space in which the conversion of the amine groups into isocyanate groups is 4 to 80% is always below the flow rate averaged over the cross-section at the start of this section.
    • 通过一种或多种芳族伯胺与气相中的光气反应制备芳族异氰酸酯。 光气和伯芳基胺在具有反应空间的反应器中在高于胺的沸点温度的温度下反应,反应空间基本上与流动方向旋转对称。 反应混合物沿着反应空间部分中基本上旋转对称的反应空间轴线的横截面平均流动,其中胺基转化为异氰酸酯基的反应空间为4-80% 不超过8米/秒。 反应混合物的横截面上的平均流量在反应空间的基本上旋转对称的反应空间的轴上,其中胺基转化为异氰酸酯基团的部分总是低于 在本节开头的横截面上平均流量。
    • 29. 发明申请
    • PROCESS FOR THE PREPARATION OF ISOCYANATES IN THE GAS PHASE
    • 在气相中制备异氰酸酯的方法
    • US20100152484A1
    • 2010-06-17
    • US12632117
    • 2009-12-07
    • Klaus BiskupRainer BrunsWolfgang LorenzFritz PohlFriedhelm SteffensVolker Michele
    • Klaus BiskupRainer BrunsWolfgang LorenzFritz PohlFriedhelm SteffensVolker Michele
    • C07C263/10
    • C07C263/10C07C265/14
    • Aromatic isocyanates are produced by reacting one or more aromatic primary amines with phosgene in the gas phase. The phosgene and primary aromatic amine(s) are reacted at a temperature above the boiling temperature of the amine(s) in a reactor having a reaction space which is essentially rotationally symmetric to the direction of flow. The flow fate, averaged over the cross-section, of the reaction mixture along the axis of the essentially rotationally symmetric reaction space in the section of the reaction space in which the conversion of the amine groups into isocyanate groups is between 4 and 80 % is not more than 8 m/sec. The flow rate averaged over the cross-section of the reaction mixture along the axis of the essentially rotationally symmetric reaction space in the section of the reaction space in which the conversion of the amine groups into isocyanate groups is 4 to 80 % is always below the flow rate averaged over the cross-section at the start of this section.
    • 通过一种或多种芳族伯胺与气相中的光气反应制备芳族异氰酸酯。 光气和伯芳基胺在具有反应空间的反应器中在高于胺的沸点温度的温度下反应,反应空间基本上与流动方向旋转对称。 反应混合物沿着反应空间部分中基本上旋转对称的反应空间轴线的横截面平均流动,其中胺基转化为异氰酸酯基的反应空间为4-80% 不超过8米/秒。 反应混合物的横截面上的平均流量在反应空间的基本上旋转对称的反应空间的轴上,其中胺基转化为异氰酸酯基团的部分总是低于 在本节开头的横截面上平均流量。