| 序号 | 专利名 | 申请号 | 申请日 | 公开（公告）号 | 公开（公告）日 | 发明人 |
|---|---|---|---|---|---|---|
| 61 | 用于在级联型湿式洗涤器内洗涤气体的方法和级联洗涤器 | CN201380065666.9 | 2013-12-20 | CN104968409A | 2015-10-07 | H·卢黑莱恩; V·卡维恩; J·萨瑞玛; P·马克拉; J·韦赫维莱宁 |
| 本发明涉及一种用于在级联型湿式洗涤器内洗涤气体的方法。在所述方法中，待要清洁的、且包含灰尘和细小杂质的气体穿过一个入口通道(11)被引入到所述级联洗涤器(10)的一个气体分配室(13)内。气体从所述气体分配室(13)穿过竖直级联管(16)向下引入到一个水储罐(14)，经净化的气体从所述水储罐(14)引入到一个微滴分离器。根据本发明，在待要清洁的气体从所述级联管(16)排放之前和/或之后，通过喷射喷嘴(20，21，22)向所述气体喷射加压的清洗液体。本发明还涉及一种级联洗涤器(10)。 | ||||||
| 62 | 一种灰肥烧制装置 | CN201410728767.6 | 2014-12-04 | CN104595913A | 2015-05-06 | 孙永剑; 张紫娟; 陶长红; 何轶超 |
| 本发明公开了一种灰肥烧制装置，旨在提供一种能有效对麦秸进行集中烧制处理，烧制过程稳定高效、可保障焚烧充分，制成的灰肥纯度高，并能对产生的烟气进行有效处理，可避免造成烟尘污染的装置。它包括焚烧窑、送料装置、净烟装置：所述的焚烧窑具有焚烧内腔，所述的焚烧窑倾斜且与水平面之间成10至60度，所述的焚烧内腔中设有由主电机带动的传动主轴，所述的传动主轴上设有多个用于拨动物料的散料体，所述的焚烧窑上设有进气口、出烟部、进料口、清料启闭门。本发明的有益效果是：分离效果上佳；可实现对烟气中固体颗粒物和粉尘的清除；利用烟气余热对原料进行干化，提高后续烧制效果；具有预热结构，能更好更充分的保证后续的焚烧。 | ||||||
| 63 | 烟雾除尘净化装置及方法 | CN201410539975.1 | 2014-10-14 | CN104275061A | 2015-01-14 | 周一帆 |
| 本发明提供一种烟雾除尘净化装置及方法。该装置包括进烟管，净化组件，喷淋组件以及排烟管。进烟管一端连接外部排烟设备，另一端连接净化组件。净化组件包括净化池和与净化池相联通的沉淀池，沉淀池内设置有冷却水。喷淋组件设置于净化池的上部，喷淋组件包括喷淋供水管和与喷淋供水管相连接的多个喷淋管，喷淋管至上而下向净化池喷射水柱。排烟管与净化池相联通。该方法包括：沉淀池内注满冷却水；烟雾经进烟管排入净化池，经沉淀池内冷却水初步冷却去除烟雾内大颗粒；喷淋组件对初步冷却后的烟雾进行冲刷，将细小粉尘冲洗至沉淀池内；冲刷后的烟雾经沉淀池内的冷却水进行再次冷却；再次冷却后的烟雾从排烟管排出进入大气。 | ||||||
| 64 | 用于处理船舶中的废气的洗涤器系统以及在船舶的洗涤器系统中处理废气的方法 | CN201280010060.0 | 2012-02-15 | CN103403312A | 2013-11-20 | A·苏米恩 |
| 本发明涉及一种利用基于水的溶液来处理船舶（1）中的废气的洗涤器系统（8），所述船舶具有船体（2）并且包括有废气源（4），所述洗涤器系统（8）包括：第一洗涤器单元（8.1）和第二洗涤器单元（8.2）；位于所述第一洗涤器单元中的废气进口（16）和位于所述第二洗涤器单元中的废气出口（26）；第二导管部分（14），该第二导管部分将所述第一洗涤器单元连接到所述第二洗涤器单元；以及第一洗涤介质回路（20）和第二洗涤介质回路（22）。所述第一洗涤介质回路（20）设置有洗涤溶液源，该洗涤溶液源包括至所述船体（2）的外部并且位于所述船舶的吃水线下方的第一连接件，并且所述第二洗涤介质回路（22）设置有洗涤溶液源，所述洗涤溶液源包括位于所述船舶中的淡水源。本发明还涉及在船舶的洗涤器系统（8）中处理废气的方法。 | ||||||
| 65 | 用于回收气体中所包含的纳米粉末和超细粉末的装置 | CN201080052135.2 | 2010-11-17 | CN102686295A | 2012-09-19 | 希查姆·马斯克洛特; 班诺特·圭扎德 |
| 本发明涉及一种用于回收气体所携载的纳米或亚微米颗粒的装置，其通过产生稳定悬浮物而回收，所述装置包括容器（3），所述容器（3）具有：用于注射液体的构件（11）；其上部位于颗粒过滤构件附近的气体排放构件（4）；以及颗粒悬浮物排出构件（9）。本发明还包括液环泵（2），以用于将气体所携载的颗粒转移并分散于液体中，所述泵包含：用于将装有纳米或亚微米颗粒的气体引入到所述泵中的构件；用于将至少一种液体注射到所述泵中的构件（15）；用于排放在所述转移之后所获得的混合物的构件。所述容器还包含用于将所述混合物引入到所述容器中的构件，以及至少一个压电小球（7），其沉浸于所述容器内，其经设计以产生微米大小的液滴雾。 | ||||||
| 66 | 用于从污染气体物流中脱除污染物的方法 | CN200880021177.2 | 2008-05-15 | CN101678259A | 2010-03-24 | H·C·哈姆里 |
| 一种用于从污染气体物流中脱除污染物例如水、CO<sub>2</sub>和/或H<sub>2</sub>S的方法，所述方法包括使气体物流流动通过具有第一和第二导管段(11，12)和任选的另外的导管段(13-15)的导管(10)，所述导管段各自包括以下部件：a)旋风流体分离段(11A-15A)，其中使气体物流形成涡流，使得污染物(11B-15B)流至分离段的外部区域，和纯化气体馏分(11C-15C)流至分离段的中心区域中；b)中心纯化气体出口管(11D-15D)，用于排出纯化气体馏分；c)外部排出管(11E-15E)，用于排出污染物；和d)文丘里管段(11F-15F)，其中使气体物流加速和降低静态压力；其中所述方法还包括：将第二导管段(12)的中心纯化气体出口管(12D)连接至第一导管段(11)的文丘里管段(11F)，从而使纯化气体馏分从第二导管段(12)流至第一导管段(11)中；将污染物吸收剂(18，贫MEG)注入第一导管段(11)的文丘里管段(11F)中；和使富含污染物和污染物吸收剂的流体馏分经过MEG循环导管(19)从第一导管段的外部排出管(11E)流至第二导管段(12)的文丘里管段(12F)中；和任选地，分别使富含污染物和污染物吸收剂的流体馏分经过另外的MEG循环导管(20、21和22)从第二、第三和第四导管段的外部排出管(12E-14E)流至第三、第四和第五导管段(13-15)的文丘里管段(13F-15F)中。 | ||||||
| 67 | 燃烧废气的处理装置 | CN01819918.6 | 2001-11-14 | CN1477989A | 2004-02-25 | 菱池通隆; 中西隆一; 中川正明; 后藤宏明 |
| 一种燃烧废气的处理装置，具有与燃烧废气的排出源连接的导向筒(21)和所供给的冷却液的暂时贮留部(22)，该导向筒(21)中的燃烧废气的入口(21a)向上开口，将该暂时贮留部(22)的冷却液出口(22a)配置在围住导向筒(21)的入口(21a)的位置，从该冷却液出口(22a)流出的冷却液，可从该导向筒(21)的入口(21a)的全周缘(21a’)沿内周面(21c’21d’)流下，利用沿该导向筒(21)的内周面(21c’、21d’)流下的冷却液，而可形成覆盖该导向筒(21)内周面(21c’、21d’)的冷却液膜。 | ||||||
| 68 | 淬冷和洗涤以及冷却和清洗热的部分氧化气体的装置和工艺 | CN98807310.2 | 1998-06-05 | CN1268070A | 2000-09-27 | 保罗·S·华莱士; 凯·A·约翰逊; 德龙姆·D·费尔 |
| 公开了一种淬冷和洗涤热的部分氧化气体并清洗和冷却热的部分氧化气体的装置。在淬冷和洗涤过程中,使用高压沉降器与洗涤塔(10)相结合有利地去除颗粒夹杂物。上述高压沉降器最好具有一个位于洗涤塔内的贮槽(18),或者同时具有位于洗涤塔内的贮槽和镇静区。采用高压沉降器可提高沉降速度并提高洗涤效率。在冷却和清洗阶段,最好使用一种具有整体清洗系统的分离罐(45)。在气化过程的冷凝和清洗阶段使用分离罐有助于从含有水蒸汽和氨的部分氧化气体中去除氨和水蒸汽。上述的分离罐(45)具有一个下部(46)和一个上部(50),并由一个传送装置(53)使上述下部与上述上部相连接,上述的上部含有一组可将水从上述上部的上端导引至上述上部的下端的塔盘(55)。上述的传送装置可使流体单向地从上述的下部流到上述的上部。 | ||||||
| 69 | 湿式排烟净化方法及其装置 | CN87106045 | 1987-07-31 | CN87106045A | 1988-03-16 | 和久井均; 清原信男; 西野晴生 |
| 本发明的湿式排烟净化方法及装置，在使第一洗涤液液面保持一定的同时，使排烟在该第一洗涤液中产生气泡进行洗涤，经洗涤的排烟再在洗涤塔中与第二洗涤液对流接触进一步洗涤，有极高的除污染效果，并且装置的结构小而简单。 | ||||||
| 70 | AN APPARATUS AND METHOD FOR PARTICULATE CAPTURE FROM GAS STREAMS AND A METHOD OF REMOVING SOLUBLE PARTICULATE FROM A GAS | US15036714 | 2014-11-14 | US20160303502A1 | 2016-10-20 | Brian Sayre HIGGINS |
| Disclosed is a method for the removal of soluble particulate matter from a gas stream, such as urea dust from the off-gas of a finishing section of a urea production plant. The method comprises subjecting the off-gas to at least two quenching stages an aqueous quenching liquid. The quenching liquid used in a first, upstream quench stage, is allowed to have a higher concentration of dissolved particulate matter than the quenching liquid in the second, downstream quench stage. The quenched gas is led through a particle capture zone, typically comprising one or more of a wet scrubber, a Venturi scrubber, and a wet electrostatic precipitator. | ||||||
| 71 | SYSTEMS AND METHODS FOR EXHAUST GAS CLEANING AND/OR BALLAST WATER TREATMENT | US14006163 | 2012-03-22 | US20140060323A1 | 2014-03-06 | Ming Liu; Nirmal Raman Gurunthalingam; Prapisala Thepsithar; Wen Sin Chong; Kok Seng Foo |
| Embodiments of the present invention relate to a system and method for efficient removal of sulfur oxides (SOx), nitrogen oxides (NOx) and particulate matter (PM) contained in an exhaust gas generated from fuel combustion and efficient treatment of water containing microorganisms (e.g. ballast water). | ||||||
| 72 | DEVICE FOR RECOVERING NANOPOWDERS AND ULTRAFINE POWDERS CONTAINED IN A GAS | US13509310 | 2010-11-17 | US20120222558A1 | 2012-09-06 | Hicham Maskrot; Benoit Guizard |
| A device for recovering nanometer or sub-micron particles carried by a gas by generating a stabilized suspension, including: a vessel including a mechanism injecting a liquid; a gas discharge mechanism in an upper portion thereof, located near a particle filter; a particle suspension outlet; and a liquid ring pump, transferring and dispersing particles carried by a gas into a liquid. The pump introduces a gas laden with nanometer or sub-micron particles into the pump; injects at least one liquid into the pump; and discharges the mixture obtained following the transfer. The vessel also includes a mechanism introducing the mixture into the vessel and at least one piezoelectric pellet, immersed in the vessel, configured to generate a fog of micron-sized droplets. | ||||||
| 73 | Flue gas washer with a supporting construction for spray pipes | US10529279 | 2002-10-05 | US07591886B2 | 2009-09-22 | Hubert Wolf; Helmut Kanka |
| Disclosed is a flue gas washer comprising a supporting construction for spray pipes used to clean at least one horizontally arranged droplet separator system. Each droplet separator system comprises droplet separator packets which are mounted on carriers. The supporting construction for the spray pipes is arranged adjacent to or between the droplet separator packets. As a result, inspection and cleaning of the separator systems can be improved significantly. | ||||||
| 74 | Device for Removing Particulate, Various Acids, and Other Contaminants from Industrial Gases | US10578541 | 2004-11-08 | US20070251393A1 | 2007-11-01 | G. Michael Pope; Jerry Green |
| Exhaust gases enter the tank of a columnar vessel (12) and are subsequently forced through a diffuser (24) that is at least partially immersed in a column of solution. | ||||||
| 75 | Wet gas stripper | US08815747 | 1997-03-12 | US06267804B1 | 2001-07-31 | G. Delane Marlowe |
| A wet gas stripper is provided for separating particulate matter entrained in a moving gas stream. The gas stripper includes a housing having a plurality of walls, and a gas inlet for receiving the moving gas stream into the housing and a gas outlet through which the moving gas stream is exhausted from the housing. A particulate collection area is formed at a base of the housing. A liquid spray element sprays a liquid against at least one of the walls of the housing above the particulate collection area to create a particulate-entraining mist. The mist defines a filtration medium for capturing the particulate matter entrained in the gas stream and carrying the particulate matter to the collection area for removal from the housing. | ||||||
| 76 | Multistep gas scrubber apparatus | US134580 | 1998-08-14 | US6102990A | 2000-08-15 | Veli Keinanen; Launo Lilja; Pekka Niemela ; Janne Ollila |
| A multiphase scrubber for the wet scrubbing of gases in several different phases comprises at least three separate basic scrubbing units so that the scrubbing of the gas is carried out in at least three, advantageously six, successive steps. The droplet separation of the scrubbed gases is carried out in a uniform cyclone-like droplet separator composed of several nested cylinders. A clean dropless gas contains a dust content below the acceptable limit. The scrubber is suited for scrubbing hot furnace gases from closed reduction furnaces. | ||||||
| 77 | Spray toner for the removal of dust from carbonization gas | US930382 | 1997-12-01 | US5948370A | 1999-09-07 | Karl-Heinz Redepenning; Andreas Schleiffer; Bernd Uckermann |
| A process for the removal of dust from gas that has been produced by low temperature carbonization is provided. The process separates solid particles by means of washing oil in a spray washer that also cools the gases that have been produced by low temperature carbonization. The process includes intensively wetting the gases that have been produced with oils that have been condensed out of the stream of the gas. At least a first and second washing stage is provided in the spray washer. The mass flow comprising the washing oil and condensate is collected in the second washing stage and subdivided. Thereafter, the mass flow is fed to both the first and second washing stage as recirculated and recycled washing oil. | ||||||
| 78 | Apparatus for purifying hot flue gas and for receiving thermal energy therefrom | US914597 | 1997-08-18 | US5840100A | 1998-11-24 | JoseP. Arencibia, Jr. |
| Particulate-containing hot flue gas flows are flowed into a boiler having a first and a second chamber. The first chamber has a gas side and a water side. The hot flue gas flows into the gas side of the first chamber which is in heat exchange relation with the water side. Steam is generated on the water side and transported to a power generator. Steam or another inert gas is periodically injected into the gas side of the first chamber for removing particulate fouling when the heat exchange relation for the gas side falls below a predetermined minimum level. Cooled flue gas leaving the gas side of the boiler is conducted to a purification chamber having spray nozzles thereby allowing large particulate to settle out of the flue gas and removing fine particulate entrained in the flue gas enabling purified flue gas to be released from an upper portion of the second chamber. | ||||||
| 79 | Venturi scrubber and method of using the same | US565022 | 1995-11-30 | US5759233A | 1998-06-02 | James J. Schwab |
| An air pollution control system incorporating a venturi scrubber and a method of cleansing a particulate-laden, contaminated gas flow are disclosed. Spray nozzles are used to introduce optimized droplets of a scrubbing liquid into the venturi to maximize particle collection efficiency. The present invention discloses automatic control systems which adjust the venturi as the properties of the effluent gases change. For example, in one embodiment, the spray volume and/or droplet size is adjusted as the particle concentration changes. In another embodiment, the spray volume is increased as the volume of effluent gas decreases. | ||||||
| 80 | Exhaust gas scrubbing process | US602136 | 1996-02-15 | US5660615A | 1997-08-26 | Ulrich Neumann; Wolfgang Willing |
| Exhaust gas is brought into contact with a washing liquid chiefly consisting of water in at least two washing stages. In the last washing stage, fresh water and/or a washing liquid containing fresh water is sprayed into the exhaust gas. In the penultimate washing stage, the exhaust gas is brought in contact with a circulating aqueous salt solution, which contains substances supplied by the exhaust gas. In the penultimate washing stage, the exhaust gas is passed through a washing zone at temperatures in the range from 30.degree. to 150.degree. C., where the quantity of aqueous salt solution passed into the washing zone per Nm.sup.3 exhaust gas flowing through the washing zone is 0.1 to 10 liters. The exhaust gas coming from the penultimate washing zone has a temperature in the range from 30.degree. to 80.degree. C., is saturated with steam for 90 to 100%, and does not contain more than 50% by weight of the dust content of the exhaust gas before the same enters the penultimate washing stage. In the last washing stage, the exhaust gas is passed through a gas-permeable, turbulence producing layer. In the last washing stage, preferably 0.05 to 2 liters washing liquid per Nm.sup.3 exhaust gas are sprayed into the exhaust gas. | ||||||
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