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    • 1. 发明授权
    • System and method for treating dust contained in extracted cement kiln combustion gas
    • 提取水泥窑燃烧气体中所含粉尘的系统和方法
    • US07749311B2
    • 2010-07-06
    • US11663393
    • 2005-09-20
    • Shinichiro SaitoKeizo Fujiwara
    • Shinichiro SaitoKeizo Fujiwara
    • B01D50/00
    • C04B7/60C04B7/436F27B7/42F27D17/008
    • A treatment system to efficiently remove lead from dust contained in extracted cement kiln combustion gas while reducing facility and running costs. A treatment system 1 comprising a probe 3 for extracting a part of combustion gas, while cooling it, from a kiln exhaust gas passage, which runs from an inlet end of a cement kiln to a bottom cyclone; a first classifier 5 for separating coarse powder from dust contained in the combustion gas extracted; a dust collector 7 for collecting dust from the extracted gas containing fine powder discharged from the first classifier 5; and a second classifier 8 for dividing dust discharged from the dust collector 7 into fine powder and coarse powder, and others. Since more lead is distributed on the fine powder side classified by the second classifier 8, lead can efficiently be removed without using chemicals and the like. The fine powder classified by the classifier 8 may be desalted by washing; high-lead-level cake obtained after the washing can be recycled; or salt water can be added to a cement mill. The coarse powder may be added to a cement grinding process or returned to cement material grinding process after the desaltation through washing.
    • 一种处理系统,可有效去除提取的水泥窑燃烧气体中含有的灰尘,同时降低设备和运行成本。 一种处理系统1,其包括用于从其从水泥窑的入口端延伸到底部旋风器的窑尾废气通道在冷却时提取一部分燃烧气体的探针3; 用于将粗粉与从所提取的燃烧气体中所含的灰尘分离的第一分级器5; 用于从包含从第一分级器5排出的细粉末的提取气体中收集灰尘的集尘器7; 以及用于将从集尘器7排出的粉尘分解成细粉末和粗粉末的第二分级器8等。 由于在由第二分级器8分类的细粉末侧分布更多的铅,因此可以在不使用化学物质等的情况下有效地除去铅。 由分级机8分类的细粉可以通过洗涤脱盐; 洗涤后获得的高铅级蛋糕可以回收利用; 或盐水可以添加到水泥磨。 可以将粗粉末加入水泥研磨过程中,或通过洗涤脱盐后返回水泥材料研磨过程。
    • 2. 发明申请
    • System and Method for Treating Dust Contained in Extracted Cement Kiln Combustion Gas
    • 提取水泥窑燃烧气体处理除尘系统及方法
    • US20080092735A1
    • 2008-04-24
    • US11663393
    • 2005-09-20
    • Shinichiro SaitoKeizo Fujiwara
    • Shinichiro SaitoKeizo Fujiwara
    • B01D49/00
    • C04B7/60C04B7/436F27B7/42F27D17/008
    • A treatment system to efficiently remove lead from dust contained in extracted cement kiln combustion gas while reducing facility and running costs. A treatment system 1 comprising a probe 3 for extracting a part of combustion gas, while cooling it, from a kiln exhaust gas passage, which runs from an inlet end of a cement kiln to a bottom cyclone; a first classifier 5 for separating coarse powder from dust contained in the combustion gas extracted; a dust collector 7 for collecting dust from the extracted gas containing fine powder discharged from the first classifier 5; and a second classifier 8 for dividing dust discharged from the dust collector 7 into fine powder and coarse powder, and others. Since more lead is distributed on the fine powder side classified by the second classifier 8, lead can efficiently be removed without using chemicals and the like. The fine powder classified by the classifier 8 may be desalted by washing; high-lead-level cake obtained after the washing can be recycled; or salt water can be added to a cement mill. The coarse powder may be added to a cement grinding process or returned to cement material grinding process after the desaltation through washing.
    • 一种处理系统,可有效去除提取的水泥窑燃烧气体中含有的灰尘,同时降低设备和运行成本。 一种处理系统1,其包括用于从其从水泥窑的入口端延伸到底部旋风器的窑尾废气通道在冷却时提取一部分燃烧气体的探针3; 用于将粗粉与从所提取的燃烧气体中所含的灰尘分离的第一分级器5; 用于从包含从第一分级器5排出的细粉末的提取气体中收集灰尘的集尘器7; 以及用于将从集尘器7排出的粉尘分解成细粉末和粗粉末的第二分级器8等。 由于在由第二分级器8分类的细粉末侧分布更多的铅,因此可以在不使用化学物质等的情况下有效地除去铅。 由分级机8分类的细粉可以通过洗涤脱盐; 洗涤后获得的高铅级蛋糕可以回收利用; 或盐水可以添加到水泥磨。 可以将粗粉末加入水泥研磨过程中,或通过洗涤脱盐后返回水泥材料研磨过程。
    • 3. 发明授权
    • Combustion gas extraction probe and combustion gas treatment method
    • US10066873B2
    • 2018-09-04
    • US10579327
    • 2004-11-16
    • Shinichiro SaitoTakahiko Suzuki
    • Shinichiro SaitoTakahiko Suzuki
    • F27D17/00F27B7/38F15D1/08
    • F27D17/001F15D1/08F27B7/38Y10T137/0318Y10T137/8766
    • [Problems] A combustion gas extraction probe that is capable of preventing burnout of a head metal portion of a probe, capable of rapidly cooling a high-temperature gas in a uniform manner in a probe, and whose outer diameter can be kept small.[Means for Solving Problems] A combustion gas extraction probe (4) having a hollow-cylindrical inner tube (4a) in which a high-temperature combustion gas flows, a hollow-cylindrical outer tube (4b) surrounding the inner tube (4a), a low-temperature gas discharge hole (4c) provided in the inner tube (4a), and a low-temperature gas supply means (9) for supplying a low-temperature gas between the inner tube (4a) and the outer tube (4b) and discharging the low-temperature gas from the discharge hole (4c) into the direction that is substantially perpendicular to the sucking direction of the high-temperature combustion gas and is toward the center of the flow of said high-temperature combustion gas. Alternatively, plural discharge holes (4c) may be provided, where the individual discharge holes (4c) are arranged at substantially the same positions from the head of the probe in the high-temperature combustion gas sucking direction, or alternatively, the discharge holes (4c) may be arranged in stages in the high-temperature combustion gas sucking direction. The flow speeds of the low-temperature gas and the high-temperature combustion gas are preferably not less than 40 m/s and not more than 100 m/s.
    • 5. 发明授权
    • Zoom lens and image pickup apparatus
    • 变焦镜头和摄像设备
    • US08564887B2
    • 2013-10-22
    • US13182072
    • 2011-07-13
    • Shinji YamasakiShinichiro Saito
    • Shinji YamasakiShinichiro Saito
    • G02B15/14
    • G02B15/177
    • A zoom lens comprising, in order from an object side to an image side, a first lens unit having a negative refractive power, a second lens unit having a positive refractive power, and a third lens unit having a positive refractive power. The second and third lens units are configured to move in an optical axis direction for a magnification variation, and the first lens unit is configured to move in the optical axis direction to reduce an image-plane fluctuation associated with the magnification variation. Expressions −0.83≦f1/f2≦−0.40 and −4.6≦f1/fw≦−2.5 T are satisfied where f1 is a focal length of the first lens unit, f2 is a focal length of the second lens unit, and fw is a focal length of the entire zoom lens at a wide angle end.
    • 一种变焦透镜,其从物体侧到像侧依次包括具有负折光力的第一透镜单元,具有正折光力的第二透镜单元和具有正折光力的第三透镜单元。 第二透镜单元和第三透镜单元被配置为沿光轴方向移动以进行放大变化,并且第一透镜单元被配置为沿光轴方向移动以减少与放大率变化相关联的图像平面波动。 满足表达式-0.83 @ f1 / f2 @ -0.40和-4.6 @ f1 / fw @ -2.5 T,其中f1是第一透镜单元的焦距,f2是第二透镜单元的焦距,fw是 整个变焦镜头在广角端的焦距。
    • 6. 发明申请
    • METHOD FOR WASHING INCINERATION ASH AND DUST CONTAINED IN EXTRACTED CEMENT KILN COMBUSTION GAS
    • 用于洗涤焚烧的方法和包含在提取的水泥窑燃烧气体中的灰尘
    • US20130199567A1
    • 2013-08-08
    • US13579160
    • 2010-02-16
    • Noritoshi TamuraShinichiro SaitoKenzaburou Kondou
    • Noritoshi TamuraShinichiro SaitoKenzaburou Kondou
    • B09B3/00
    • B09B3/00B01D21/01B01D2247/04C02F1/004C02F1/70C02F2101/20C02F2103/18C04B18/06C04B18/062C04B20/023Y02W30/92
    • To minimize harmful effects on operation due to scale adhesion while accommodating increase in the amount of generated chlorine bypass dust and suppress facility cost and running cost including medical agent cost low when incineration ash and dust contained in extracted cement kiln combustion gas are subject to water treatment.[Means for Solving Problems] A water treatment system 1 comprising: a dissolution tank 32 for dissolving a fly ash A in a water W; a dissolution tank 22 for dissolving a dust D contained in combustion gas extracted from a kiln exhaust gas passage running from an inlet end of a cement kiln to a bottom cyclone in a water W; and a vertical filter press 11 for separately filtering a slurry S2 fed from the dissolution tank 32 and a slurry S1 fed from the dissolution tank 22 from each other. It is possible to install water treatment facilities 33-35 for a filtrate L3 of the slurry containing fly ash discharged from the vertical filter press, and water treatment facilities 23-27 for a filtrate L1 of the slurry containing ash discharged from the filtering device.
    • 为了尽可能减少由于附着垢而导致的对操作的有害影响,同时适应生成的氯旁路粉尘量的增加,并且抑制提取的水泥窑燃烧气体中包含的焚烧灰和粉尘经受水处理时,包括医药成本低的设备成本和运行成本 。 解决问题的手段一种水处理系统1,包括:用于将粉煤灰A溶解在水W中的溶解槽32; 溶解槽22,用于将从水泥窑的入口端延伸的窑尾废气通道提取的燃烧气体中所含的粉尘D溶解到水W中的底部旋风分离器; 以及用于分别过滤从溶解槽32供给的浆料S2和从溶解槽22供给的浆料S1的立式压滤机11。 对于从立式压滤机排出的含有飞灰的浆液的滤液L3和从过滤装置排出的含有灰的浆料的滤液L1的水处理设备23-27,可以安装水处理设备33-35。
    • 7. 发明授权
    • Zoom lens and image pickup apparatus having the zoom lens
    • 具有变焦镜头的变焦镜头和摄像装置
    • US08390936B2
    • 2013-03-05
    • US13086153
    • 2011-04-13
    • Shinichiro SaitoNobuyuki MiyazawaTomonori Kimura
    • Shinichiro SaitoNobuyuki MiyazawaTomonori Kimura
    • G02B15/14H04N5/225
    • G02B15/173
    • A zoom lens includes, in order from an object side to an image side, a first lens unit having a positive refractive power, a second lens unit having a negative refractive power, a third lens unit having a positive refractive power, and a rear lens unit including one or more lens units. An interval between respective adjacent lens units varies during zooming such that an interval between the first lens unit and the second lens unit is larger at a telephoto end than at a wide-angle end and an interval between the second lens unit and the third lens unit is smaller at the telephoto end than at the wide-angle end. The third lens unit includes at least one negative lens. An Abbe number (νd3n) and a relative partial dispersion (θgF3n) of a material of the negative lens are appropriately set based on predetermined conditional expressions.
    • 变焦透镜从物体侧到像侧依次包括具有正屈光力的第一透镜单元,具有负屈光力的第二透镜单元,具有正折光力的第三透镜单元和后透镜 单元包括一个或多个透镜单元。 各相邻透镜单元之间的间隔在变焦期间变化,使得第一透镜单元和第二透镜单元之间的间隔在远摄端处比在广角端处较大,并且第二透镜单元与第三透镜单元之间的间隔 在远摄端比在广角端小。 第三透镜单元包括至少一个负透镜。 基于预定的条件表达式适当地设置负透镜的材料的阿贝数(&ngr; d3n)和相对部分色散(& gf3n)。
    • 8. 发明授权
    • Apparatus and method for adding wet ash to cement
    • 将灰渣添加到水泥中的设备和方法
    • US08282263B2
    • 2012-10-09
    • US12088932
    • 2006-10-17
    • Shinichiro Saito
    • Shinichiro Saito
    • B28C5/00
    • C04B7/26C04B7/52Y02P40/145
    • An apparatus and a method for adding wet ash to cement which make it possible to fed wet ash to a cement mill without generating cost for drying the wet ash and new setting space at the neighboring area of the entrance portion of the cement mill. The apparatus comprises a dewaterer for dewatering wet ash, a mixer 7 for mixing the wet ash with one of materials that are mixed with clinker and ground together, and a feeder 11 for feeding the mixture to a cement mill 14. After dewatered, the wet ash with predetermined quantity is mixed with the one of the materials that are mixed with clinker and ground together and fed to the mill. The water content of the wet ash after dewatered is adjusted to 20 mass percent or below, preferably to 15 mass percent or below. A centrifugal separator can be used as the dewaterer, and a pug mill may be used as the mixer. Modified ash (fly ash slurry) from fly ash decarbonization facilities can effectively be used as the wet ash by feeding it to the cement mill.
    • 一种用于向水泥中加入湿灰的装置和方法,其可以将湿灰分送入水泥磨而不产生用于干燥湿灰的成本和在水泥磨的入口部分的相邻区域的新的设置空间。 该装置包括用于将湿灰分脱水的脱水器,用于将湿灰与将其与熟料混合并研磨在一起的材料之一混合的混合器7以及用于将混合物供给到水泥磨机14的进料器11.脱水后, 将预定量的灰与与熟料混合并一起研磨并进料到研磨机中的一种材料混合。 脱水后的湿灰分含水量调整为20质量%以下,优选为15质量%以下。 可以使用离心分离器作为脱水器,并且搅拌机可以用作搅拌机。 来自飞灰脱碳设备的改性灰(粉煤灰)可以通过将其送入水泥厂而被有效地用作湿灰。
    • 10. 发明申请
    • Combustion gas extraction probe and combustion gas treatment method
    • 燃烧气体提取探针和燃烧气体处理方法
    • US20110083745A1
    • 2011-04-14
    • US10579327
    • 2004-11-16
    • Shinichiro SaitoTakahiko Suzuki
    • Shinichiro SaitoTakahiko Suzuki
    • F15D1/00
    • F27D17/001F15D1/08F27B7/38Y10T137/0318Y10T137/8766
    • [Problems] A combustion gas extraction probe that is capable of preventing burnout of a head metal portion of a probe, capable of rapidly cooling a high-temperature gas in a uniform manner in a probe, and whose outer diameter can be kept small.[Means for Solving Problems] A combustion gas extraction probe (4) having a hollow-cylindrical inner tube (4a) in which a high-temperature combustion gas flows, a hollow-cylindrical outer tube (4b) surrounding the inner tube (4a), a low-temperature gas discharge hole (4c) provided in the inner tube (4a), and a low-temperature gas supply means (9) for supplying a low-temperature gas between the inner tube (4a) and the outer tube (4b) and discharging the low-temperature gas from the discharge hole (4c) into the direction that is substantially perpendicular to the sucking direction of the high-temperature combustion gas and is toward the center of the flow of said high-temperature combustion gas. Alternatively, plural discharge holes (4c) may be provided, where the individual discharge holes (4c) are arranged at substantially the same positions from the head of the probe in the high-temperature combustion gas sucking direction, or alternatively, the discharge holes (4c) may be arranged in stages in the high-temperature combustion gas sucking direction. The flow speeds of the low-temperature gas and the high-temperature combustion gas are preferably not less than 40 m/s and not more than 100 m/s.
    • [问题]能够防止探头的头部金属部分的烧坏,能够以均匀的方式在探头中快速冷却高温气体并且其外径可以保持较小的燃烧气体提取探针。 解决问题的手段具有高温燃烧气体流过的中空圆柱形内管(4a)的燃烧气体提取探针(4),围绕内管(4a)的中空圆柱形外管(4b) 设置在内管(4a)中的低温气体排出孔(4c)和用于在内管(4a)和外管(...)之间供给低温气体的低温气体供给装置(9) 4b),并且将排出孔(4c)的低温气体排出到与高温燃烧气体的吸引方向大致正交的方向,并朝向高温燃烧气体的流动的中心。 或者,也可以设置多个排出孔(4c),在各个排出孔(4c)配置在与高温燃烧气体吸入方向的探头的头部大致相同的位置,或者,排出孔 4c)可以在高温燃烧气体吸入方向上分阶段地布置。 低温气体和高温燃烧气体的流速优选为40m / s以上且100m / s以下。