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    • 1. 发明授权
    • Wood drying plant and a method of purifying a drying gas from a wood
drying device
    • 木材干燥设备和从木材干燥装置中净化干燥气体的方法
    • US5966837A
    • 1999-10-19
    • US851627
    • 1997-05-06
    • Stefan BackaUlf Persson
    • Stefan BackaUlf Persson
    • B01D5/00B01D53/00F26B25/00F26B3/00
    • B01D5/0054B01D53/002F26B25/006B01D2257/708B01D2257/80F26B2210/16
    • The device relates to a wood drying plant comprising a wood drying device and a purifying device which is arranged to receive a drying gas from the wood drying device, the drying gas comprising water steam and volatilized organic components such as terpenes, and to purify the drying gas from organic components and to recover the latter. The purifying device comprises at least one condenser which is arranged to separate relatively difficultly volatilized components containing organic components and relatively easily volatilized components. The purifying device also comprises a separating device which is arranged to separate said organic components and a rest material from the relatively difficultly volatilized components. The purifying device also comprises a transferring device which is arranged to transfer organic components present in the rest material to the drying gas introduced in the purifying device.
    • 该装置涉及一种木材干燥设备,其包括木材干燥装置和净化装置,其被设置成从木材干燥装置接收干燥气体,所述干燥气体包括水蒸汽和挥发的有机组分如萜烯,并且净化干燥 从有机成分中吸收气体并回收。 净化装置包括至少一个冷凝器,其布置成分离含有有机组分的相对难挥发的组分和相对容易挥发的组分。 净化装置还包括分离装置,其被布置成将所述有机组分和剩余材料与相对难挥发的组分分离。 净化装置还包括转移装置,其被设置成将存在于其余材料中的有机成分转移到引入净化装置的干燥气体。
    • 2. 发明授权
    • Poppet damper in exhaust gas duct
    • 排气管中提升阻尼器
    • US5738337A
    • 1998-04-14
    • US809780
    • 1997-04-15
    • Satoshi Yamazaki
    • Satoshi Yamazaki
    • F23L13/00F16K1/36F16K1/32
    • F16K1/36
    • The present invention provides a poppet damper, disposed in an exhaust gas duct, which makes it possible to perform an easy machining for providing a sealing surface and which provides excellent sealing following deformation caused by heat. The poppet damper includes a damper seat, disposed in a duct casing; a poppet plate for controlling exhaust gas flow by adjustment of a gap between the poppet plate and the damper seat; and an air cylinder and a damper shaft for allowing driving of the aforementioned poppet plate in a reciprocating manner. A seal plate is mounted to the poppet plate (3), which seal plate is separated by a gap of predetermined size from the poppet plate, with the seal plate placed in contact with the damper seat when the damper is closed.
    • PCT No.PCT / SE95 / 01086 Sec。 371日期1997年04月15日 102(e)1997年4月15日PCT PCT 1995年9月25日PCT公布。 公开号WO96 / 10144 日期:1996年04月4日本发明提供了一种设置在废气管道中的提升阀阻尼器,其能够进行容易的加工以提供密封面,并且在由热引起的变形后提供优异的密封。 所述提升阻尼器包括设置在管壳中的阻尼器座; 提升板,用于通过调节提升板和阻尼器座之间的间隙来控制废气流; 以及用于允许以往复方式驱动上述提升板的气缸和减震器轴。 密封板安装在提升板(3)上,该密封板通过预定尺寸的间隙与提升板隔开,当阻尼器关闭时,密封板与阻尼器座接触。
    • 3. 发明授权
    • Method and device for separating heavy particles from a particulate
material
    • 从颗粒材料分离重颗粒的方法和装置
    • US5725102A
    • 1998-03-10
    • US553508
    • 1995-11-30
    • Lennart Gustavsson
    • Lennart Gustavsson
    • B07B7/086B07B9/02B07B7/04
    • B07B9/02B07B7/0865
    • In a method for separating heavy particles from a particulate material containing such heavy particles, use is made of a device having a Coanda sifter, which is adapted to receive a flow of the particulate material and which has a downwardly-facing, convexly single-curved surface (9), and a zigzag sifter (13) arranged after the Coanda sifter and having a plurality of zig-zag-shaped vertical walls (14) which are perpendicular to the axis of curvature of the single-curved surface (9) and define between them channels (15) extending upwards in zig-zag fashion. The particulate material is transported to the Coanda sifter and is conducted over its convexly single-curved surface (9) to have imparted to it a direction of motion (P1, P2) which is dependent on the weight of the particles and in which the particles are guided into the zigzag sifter (13). The particles are guided into the channels (15) of the zigzag sifter (13) in the lower portions thereof and from the side parallel to the channel walls (14). The particles are transported up through the channels (15) with the aid of a flow of transport air which is so adjusted that the heavy particles are separated in the zigzag sifter. (13).
    • PCT No.PCT / SE94 / 00591 Sec。 371日期:1995年11月30日 102(e)1995年11月30日日期PCT PCT 1996年6月16日PCT公布。 公开号WO95 / 00261 日期1995年1月5日在一种用于从含有这种重颗粒的颗粒材料中分离重质颗粒的方法中,使用具有柯恩筛子的装置,该装置适于接纳颗粒材料的流动并且具有向下 ,凸形单曲面(9)以及设置在附件筛分器之后的锯齿形筛子(13),并且具有多个锯齿形垂直壁(14),其垂直于单曲线 表面(9)并且在它们之间限定以锯齿形方式向上延伸的通道(15)。 颗粒材料被运送到附件筛分器并且在其凸形单曲面(9)上传导以赋予它一个取决于颗粒重量的运动方向(P1,P2),其中颗粒 被引导到锯齿筛(13)。 颗粒被引导到锯齿形筛子(13)在其下部和平行于通道壁(14)的一侧的通道(15)中。 借助于如此调节的输送空气流将颗粒向上传送通过通道(15),使得重颗粒在Z字形筛子中分离。 (13)。
    • 4. 发明授权
    • Device for recuding the effects of the tendency of a paper web to adhere
to a drying cylinder in a papermaking machine
    • 用于回收纸幅粘附在造纸机中的干燥筒的趋势的影响的装置
    • US5711088A
    • 1998-01-27
    • US765195
    • 1997-01-28
    • Niclas LindqvistClaes Halldin
    • Niclas LindqvistClaes Halldin
    • D21F5/04D21G5/00
    • D21F5/042
    • A device is arranged in the drying section of a papermaking machine for reducing the effects of the tendency of a paper web (4) to adhere to a drying cylinder (1) as it passes from the drying cylinder to a subsequent guide roll (2). In the drying section, the paper web (4), supported by a drying fabric (5), is conducted alternatingly over a plurality of drying cylinders (1) and guide rolls (2). A blow box (6) is arranged in the transition portion (A) and has a wall (7) extending in parallel with the drying fabric (5) so as to form a narrow air gap (8) between the wall and the drying fabric. The blow box (6) comprises nozzle (12) having a slot-shaped opening for ejecting a well-defined air jet (P1) towards the drying fabric (5) away from the air gap (8). The nozzle (12) is directed such that its center plane intersects the circumferential surface of the drying cylinder (1) along a first straight line positioned upstream of a second line, along which the paper web (4) leaves the drying cylinder (1).
    • PCT No.PCT / SE95 / 00752 Sec。 371日期1997年1月28日 102(e)日期1997年1月28日PCT提交1995年6月20日PCT公布。 出版物WO96 / 01341 日期1996年1月18日在造纸机的干燥部中设置有一个装置,用于减少纸幅(4)在干燥筒(1)从干燥滚筒经过干燥筒 导辊(2)。 在干燥部分中,由干燥织物(5)支撑的纸幅(4)交替地在多个干燥筒(1)和导向辊(2)上进行。 吹风箱(6)布置在过渡部分(A)中并且具有与干燥织物(5)平行延伸的壁(7),以便在壁和干燥织物之间形成狭窄的气隙(8) 。 吹风箱(6)包括具有槽形开口的喷嘴(12),用于将远离气隙(8)的干燥织物(5)排出明确的空气射流(P1)。 喷嘴(12)被定向为使得其中心平面沿着位于第二线上游的第一直线与干燥筒(1)的圆周表面相交,纸幅沿着该第二直线离开干燥筒(1) 。
    • 5. 发明授权
    • Apparatus for cleaning gas
    • 清洁气体的设备
    • US5641124A
    • 1997-06-24
    • US411835
    • 1995-03-30
    • Nils Bringfors
    • Nils Bringfors
    • B01D53/50B05B7/04B05B7/06B05B7/08B05B1/28
    • B05B7/066B01D53/504B05B7/0466B05B7/0807
    • A nozzle (12a, 12b, 12c) for atomizing a liquid, optionally containing suspended dry matter, through use of compressed gas, comprises, an inlet (32b) for liquid, an inlet (31b) for compressed gas, and an outlet (41) for gas mixed with finely divided liquid, as well as an intermediate mixing space (51). The inlet (31b) for compressed gas is adapted to give the gas a substantially rectilinear path through the mixing space (51). The inlet (32b) for the liquid is separated from the mixing space (51) by a partition (32) having a plurality of first holes (38) for introducing the liquid into the mixing space (51) in a direction substantially perpendicular to the main flow direction of the gas in the mixing space (51). The mixing space (51) is defined downstream by a wall (35) having a plurality of second holes (39). An inlet device (11a, 11b, 11c) comprising the inlet (31b) for compressed gas and the inlet (32b) for liquid consists of two concentric tubes (31, 32). The inlet (32b) for liquid consists of the inner tube (32). The inlet (31b) for compressed gas consists of the annular conduit (31b) between the concentric tubes (31, 32). The inner tube (32) is closed in the axial direction downstream of the first holes (38) provided for introducing the liquid into the mixing space (51). A convergent channel (57) connects the mixing space (51) to the outlet (41).
    • PCT No.PCT / SE93 / 00810 Sec。 371日期1995年3月30日 102(e)1995年3月30日PCT 1993年10月6日PCT PCT。 出版物WO94 / 08700 日期1994年04月28日用于通过使用压缩气体雾化任选地含有悬浮干物质的液体的喷嘴(12a,12b,12c)包括:用于液体的入口(32b),用于压缩气体的入口(31b) 和用于与细碎液体混合的气体的出口(41)以及中间混合空间(51)。 用于压缩气体的入口(31b)适于使气体通过混合空间(51)的基本上直线的路径。 用于液体的入口(32b)通过具有多个第一孔(38)的分隔件(32)与混合空间(51)分开,用于将液体沿基本垂直于 气体在混合空间(51)中的主流动方向。 混合空间(51)由具有多个第二孔(39)的壁(35)限定在下游。 包括用于压缩气体的入口(31b)和用于液体的入口(32b)的入口装置(11a,11b,11c)由两个同心管(31,32)组成。 用于液体的入口(32b)由内管(32)组成。 用于压缩气体的入口(31b)由在同心管(31,32)之间的环形导管(31b)组成。 内管(32)在用于将液体引入混合空间(51)中的第一孔(38)的下游沿轴向封闭。 收敛通道(57)将混合空间(51)连接到出口(41)。
    • 6. 发明授权
    • Method and apparatus for cleaning a gas
    • 用于清洁气体的方法和装置
    • US5582634A
    • 1996-12-10
    • US403863
    • 1995-03-24
    • Vassilis Burdis
    • Vassilis Burdis
    • B01D53/14B01D53/64B01D53/68C01B7/07B01D3/00
    • B01D53/1418B01D53/64B01D53/68C01B7/0712
    • A method and an apparatus for cleaning a gas containing pollutants, such as hydrogen chloride and heavy metals, are described. The polluted gas (2) is contacted with an aqueous washing liquid (3) in a scrubber (1), whereupon part of the washing liquid is preevaporated in a preevaporation unit (7) to form a hydrochloric-acid-containing top fraction, which is essentially free from heavy metals, and a bottom fraction containing hydrochloric acid and heavy metals. Part of the bottom fraction is recirculated (15) for renewed preevaporation, while the remainder of the bottom fraction is treated (16) to remove any heavy metals present. The top fraction from the preevaporation is distilled in a rectification unit (22) to form a top fraction (31) and a bottom fraction (35).
    • PCT No.PCT / SE93 / 00606 Sec。 371日期:1995年3月24日 102(e)1995年3月24日PCT PCT 1993年7月1日PCT公布。 公开号WO94 / 07590 日期1994年04月14日描述了一种用于清洁含有污染物的气体如氯化氢和重金属的方法和装置。 将污染气体(2)与洗涤器(1)中的水性洗涤液(3)接触,于是部分洗涤液体在一个预蒸发单元(7)中被蒸发,形成含盐酸的顶部馏分 基本上不含重金属,而含有盐酸和重金属的底部馏分。 底部部分的一部分被再循环(15)以用于更新的初步蒸发,而底部馏分的其余部分被处理(16)以除去存在的任何重金属。 在精馏单元(22)中蒸馏来自蒸发蒸发的顶部馏分以形成顶部馏分(31)和底部馏分(35)。
    • 7. 发明授权
    • Device for cleaning filter elements
    • 过滤元件清洗装置
    • US06022388A
    • 2000-02-08
    • US91056
    • 1998-06-09
    • Bernt AnderssonUlf Alterby
    • Bernt AnderssonUlf Alterby
    • B01D29/66B01D46/00B01D46/04
    • B01D46/04B01D46/0068
    • A device for cleaning filter elements, such as filter bags, having upper open ends, in a filter installation for filtering polluted gas. The gas passing, during operation, from the outside and through said filter elements, in which installation filter elements are juxtaposed in a plurality of essentially parallel rows. The device includes an essentially horizontal distribution pipe, which extends essentially in parallel with the rows of filters elements and is adapted to be connected to a pressure medium source via a valve. The device further includes a plurality of nozzle elements, which are connected to the distribution pipe. The nozzle elements are adapted to direct pressure medium pulses into the upper open ends of the filter elements in at least two juxtaposed rows of filter elements.
    • PCT No.PCT / SE97 / 00100 Sec。 371日期1998年6月9日第 102(e)1998年6月9日PCT 1997年1月22日PCT PCT。 第WO97 / 26976号公报 日期1997年7月31日用于过滤污染气体的过滤器装置中用于清洁过滤元件的装置,例如具有上开口端的过滤袋。 在操作期间,气体从外部通过所述过滤器元件,其中安装过滤器元件以多个基本平行的行并列。 该装置包括基本上水平的分配管,其基本上与排列的过滤器元件平行地延伸,并且适于经由阀连接到压力介质源。 该装置还包括多个喷嘴元件,其连接到分配管。 喷嘴元件适于将压力介质脉冲引导到至少两个并排的过滤元件行中的过滤元件的上开口端。
    • 8. 发明授权
    • Cyclone
    • 气旋
    • US5917065A
    • 1999-06-29
    • US952449
    • 1997-11-20
    • Claes HalldinLars-Erik JohanssonHeikki Salo
    • Claes HalldinLars-Erik JohanssonHeikki Salo
    • B01D45/12B04C20060101B04C5/12B04C5/13
    • B04C5/13B01D45/12
    • A cyclone for treating a gas flow (F) containing dust comprises a cyclone chamber (1) of circular cross section and having a vertical axis, and a central tube (7) of circular cross section, which is coaxially arranged in the upper portion of the cyclone chamber (1). An elongated insert element (10), which is vertically inserted in the central tube (7), is so designed and extends in such a manner downwards in the central tube (7) from the upper end thereof that a circumferential gap (17) exists between the insert element (10) and the central tube (7). This gap (17) has a preferably constant cross-sectional area which does not increase in the direction of the gas flow.
    • PCT No.PCT / SE95 / 00607 Sec。 371日期:1997年11月20日 102(e)1997年11月20日日期PCT提交1995年5月30日PCT公布。 WO96 / 38231 PCT公开号 日期1996年12月5日用于处理含有灰尘的气流(F)的旋风分离器包括圆形横截面的旋风室(1)和垂直轴线,以及圆形截面的中心管(7),其同轴布置 在旋风室(1)的上部。 垂直插入中心管(7)中的细长的插入元件(10)被设计成在中心管(7)中从其上端向下延伸,使其周向间隙(17)存在 在插入元件(10)和中心管(7)之间。 该间隙(17)具有在气流方向上不增加的优选恒定的横截面面积。
    • 10. 发明授权
    • Method for separating substances from a gaseous medium by dry adsorption
    • US5885539A
    • 1999-03-23
    • US836718
    • 1997-06-09
    • Odd E. Bjarn.o slashed.Geir Wedde
    • Odd E. Bjarn.o slashed.Geir Wedde
    • B01D53/08B01D53/10B01D53/68B01D53/83C01B7/20C25C3/22
    • C25C3/22B01D53/10B01D53/68B01D53/83
    • The treatment, through a dry adsorption process, of a gas from a hot electrolytic process for aluminum production comprises at least two stages. Particulate aluminum oxide (the adsorbent) passes through the stages of the adsorption process countercurrently to the gas. Thus, the gas is treated with a partly spent adsorbent in a first dry adsorption stage, whereupon the particulate adsorbent is separated from the gas downstream from the first adsorption stage. Part of the separated particulate adsorbent is removed from the adsorption process for recycling adsorbed fluorine-containing substances to the electrolytic process. The remainder of the separated adsorbent is recirculated in the first adsorption stage in order to optimize the adsorption of fluorine-containing substances and the desorption of sulfur dioxide from the aluminum oxide in this stage. Simultaneously, the gas is transferred to a second dry adsorption stage. In this second stage, the gas is treated with essentially unspent, reactive particulate aluminum oxide, so that any gaseous fluoride remaining in the gas is very efficiently adsorbed, while at the same time a substantial part of the sulfur dioxide in the gas is also adsorbed. Finally, this particulate aluminum oxide is separated from the gas downstream from the second dry adsorption stage, before the gas is discharged into the surrounding atmosphere. The separated aluminum oxide is transferred to the first adsorption stage, optionally after passing a desorption stage for the removal of the adsorbed sulfur dioxide in order to reduce the discharges of sulfur dioxide from the aluminum production. The separation of sulphur dioxide in the second adsorption stage is improved by recycling, to the second adsorption stage, aluminum oxide having undergone the desorption treatment.