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    • 21. 发明申请
    • Device and method for processing combustion exhaust gas
    • 燃烧废气处理装置及方法
    • US20070086930A1
    • 2007-04-19
    • US10561479
    • 2004-06-28
    • Shinichiro Saito
    • Shinichiro Saito
    • B01D53/94B01D53/34B01D53/56B01D50/00
    • B01D53/8625B01D53/64B01D53/8621B01D53/8662B01D2251/104B01D2251/108
    • [Problems] To suppress an increase in the discharge amount of harmful substances and operating cost in a cement kiln or the like. [Means for Solving Problems] This combustion exhaust gas G processing device comprises a dust collector 6 collecting dust in combustion exhaust gas G, a wet dust collector 7 collecting water soluble components and dust in the combustion exhaust gas G passed through the dust collector 6, and a catalyst tower 12 decomposing and removing NOx and/or dioxins in the combustion exhaust gas G passed through the wet dust collector 7. The device also desirably comprises a reheater 11 heating the combustion exhaust gas G discharged from the wet dust collector 7 at the front stage of the catalyst tower 12, an oxidizer adding device 10 adding an oxidizer to the combustion exhaust gas G passed through the dust collector 6, a solid/liquid separator 16 separating slurry discharged from the wet dust collector 7 into solid and liquid phases, a mercury adsorbing tower 17 adsorbing mercury in liquid separated in the solid/liquid separator 16, and a heat recovering device 13 heating the combustion exhaust gas G discharged from the catalyst tower 12 at the rear stage of the catalyst tower 12.
    • [问题]抑制水泥窑等中的有害物质的排出量和运行成本的增加。 [解决问题的方法]该燃烧废气G处理装置包括收集燃烧废气G中的灰尘的集尘器6,收集通过集尘器6的燃烧废气G中的水溶性成分和灰尘的湿式集尘器7, 以及催化塔12,其分解和除去通过湿式除尘器7的燃烧废气G中的NOx和/或二恶英。该装置还期望地包括再加热器11,其加热从湿式除尘器7排出的燃烧废气G 催化剂塔12的前段,向通过集尘器6的燃烧废气G添加氧化剂的氧化剂添加装置10,将从湿式除尘器7排出的浆料分离成固相和液相的固/液分离器16, 将固体/液体分离器16中分离的液体中的汞吸附在汞吸附塔17上,以及加热燃烧废气的热回收装置13 气体G在催化塔12的后段从催化剂塔12排出。
    • 23. 发明授权
    • Optical pick-up apparatus and correction lens for use in the apparatus
    • 用于该装置的光学拾取装置和校正透镜
    • US07170844B2
    • 2007-01-30
    • US10893969
    • 2004-07-20
    • Shinichiro Saito
    • Shinichiro Saito
    • G11B7/00
    • G11B7/1376G11B7/1374G11B7/1378G11B7/1381G11B7/139G11B7/13925G11B7/13927G11B2007/0006
    • In an optical pick-up apparatus for recording to or reproducing from an optical information recording medium, the optical pick-up apparatus includes: a light source for emitting light flux; a light converging optical system having an aperture and an objective lens and converging the light flux emitted from the light source on the optical information recording medium; a photodetector for detecting light reflected from the optical information recording medium; and a driving section for driving the objective lens and the aperture in association with the objective lens. A non-parallel light is incident on the objective lens, the light converging optical system includes a first part and a second part which is more apart from an optical axis of the light converging optical system than the first part, and the light flux passed through the first part is converged on an information recording surface of the optical information recording medium through a transparent substrate of the optical information recording medium so that a wavefront aberration on the information recording surface is not more than 0.07 λ rms, and the light flux passed through the second part generates a spherical aberration.
    • 在用于记录到光学信息记录介质或从光学信息记录介质再现的光学拾取装置中,光学拾取装置包括:用于发射光通量的光源; 具有孔径和物镜的聚光光学系统,并将从光源发射的光束会聚在光学信息记录介质上; 光检测器,用于检测从光信息记录介质反射的光; 以及与物镜相关联地驱动物镜和孔的驱动部。 非平行光入射到物镜上,聚光光学系统包括第一部分和第二部分,其比聚光光学系统的光轴比第一部分更远,并且光通量通过 第一部分通过光学信息记录介质的透明基板会聚在光学信息记录介质的信息记录表面上,使得信息记录表面上的波前像差不大于0.07λrms,并且光通量通过 第二部分产生球面像差。
    • 24. 发明授权
    • Optical pickup apparatus and objective lens
    • 光学拾取装置和物镜
    • US07102980B2
    • 2006-09-05
    • US09983682
    • 2001-10-25
    • Shinichiro SaitoKatsuya Sakamoto
    • Shinichiro SaitoKatsuya Sakamoto
    • G11B7/135
    • G11B7/1353G11B7/1374G11B7/13922G11B2007/0006
    • An objective lens of an optical pickup apparatus converges a divergent light flux onto an information recording surface. The following conditional formula is satisfied: |δSA1/δU|·|δU|+|δSA2/δT|·|δT|≦0.07 λrms where λ represents a wavelength of a light source, δSA1/δU represents a change of a spherical aberration for an object-to-image distance change δU (|δU|≦0.5 mm) and δSA2/δT represents a change of spherical aberration for a temperature change δT (|δT|≦30° C.), the object-to-image distance is a distance between the light source (a light emitting point) and the information recording surface.
    • 光学拾取装置的物镜将发散光束会聚到信息记录表面上。 满足以下条件公式:<?in-line-formula description =“In-line Formulas”end =“lead”?> | deltaSA /deltaU|.|deltaU|+|deltaSA < SUB> 2 / deltaT |。| deltaT | <= 0.07 lambdarms <?in-line-formula description =“In-line Formulas”end =“tail”?>其中lambda表示光源的波长, deltaSA&lt; 1&gt; / deltaU表示对象到图像间距变化ΔU(| deltaU |≤0.5mm)和deltaSA2 / deltaT表示的球面像差的变化 对于温度变化ΔT(| deltaT | <= 30℃)的球面像差的变化,对象间距离是光源(发光点)和信息记录面之间的距离。
    • 30. 发明授权
    • Industrial salt and apparatus and process for producing industrial salt
    • 工业盐和工业盐的生产工艺和工艺
    • US08808651B2
    • 2014-08-19
    • US13128183
    • 2009-04-15
    • Noritoshi TamuraShinichiro SaitoYoshinobu Tatsumi
    • Noritoshi TamuraShinichiro SaitoYoshinobu Tatsumi
    • B01D47/00B01D53/46B01D53/56B01D53/86B01J8/00
    • C04B7/60C01D1/02C01D3/08C01D3/14
    • To provide a low price industrial salt by reducing facility and operation costs without electro-deposition and crystallization and through reduction in quantity of chemicals used. An industrial salt S obtained by the steps of: extracting a part of combustion gas from a kiln exhaust gas passage running from an inlet end 12b of a cement kiln 12 to a bottom cyclone 13; recovering dust D from the extracted gas G2 and washing recovered dust; and drying a filtrate L1 after the washing in a gas stream. The industrial salt can be obtained by removing a calcium component from the filtrate and drying the filtrate from which the calcium component is removed in a gas stream. Further, from the filtrate can be removed sulfate radical, and drying the filtrate from which the calcium component is removed in a gas stream to obtain the industrial salt. For the drying can be used an exhaust gas discharged from a clinker cooler 12a and a spray drier 43 may be used for the drying. Drying in a stream provides industrial salt whose particle size is larger or equal to 20 μm and smaller or equal to 500 μm.
    • 通过降低设备和运行成本,无需电沉积和结晶,并通过减少化学品的使用量来提供低价格的工业盐。 通过以下步骤获得的工业盐S:从从水泥窑12的入口端12b延伸到底部旋风分离器13的窑尾废气通道中提取一部分燃烧气体; 从提取的气体G2回收灰尘D并洗涤回收的灰尘; 并在气流中洗涤后将滤液L1干燥。 可以通过从滤液中除去钙成分并干燥在气流中除去钙成分的滤液来获得工业盐。 此外,从滤液中可以除去硫酸根,并在气流中干燥除去钙成分的滤液,得到工业盐。 为了干燥,可以使用从熟料冷却器12a排出的排气,并且可以使用喷雾干燥器43进行干燥。 在流中干燥提供粒度大于或等于20μm且小于或等于500μm的工业盐。