| 序号 | 专利名 | 申请号 | 申请日 | 公开（公告）号 | 公开（公告）日 | 发明人 |
|---|---|---|---|---|---|---|
| 181 | Tower for treating gas | JP1470282 | 1982-02-01 | JPS57147423A | 1982-09-11 | RICHIYAADO CHIYAARUZU DAATON |
| 182 | JPS575064Y2 - | JP2632178 | 1978-03-03 | JPS575064Y2 | 1982-01-30 | |
| 183 | JPS5561422U - | JP14616678 | 1978-10-24 | JPS5561422U | 1980-04-26 | |
| Apparatus for continuously removing fine dust particles from gases, comprising a single stage or a plurality of stages each stage comprising a tray (5) having one or more slit(s) or hole(s) (6) and a baffle plate (7) installed beneath the tray, a gas inlet port (1) for introducing a gas containing fine dust particles and a water inlet port (2) or introducing washing water onto the first stage tray whereby the gas and liquid travel together along each tray and are injected from said slit(s) or hole(s) so as to impinge upon the baffle plate. | ||||||
| 184 | Gas-liquid contact device | JP5263878 | 1978-05-04 | JPS54145371A | 1979-11-13 | KOBAYASHI AKIO; YAGUCHI KUNIHIDE; TAKAIWA MASAKAZU |
| PURPOSE: Rod type fillers with diameters of less than 50mm are filled in a gas-liquid contact device in parallel and horizontal direction in a range of 2 to 30% packing ratio, whereby gas phase material transfer coefficient is increased by contact area increase and pressure loss decrease. CONSTITUTION: Rod type fillers 2 with diameters of less than 50mm are filled inside the gas-liquid contact device 1 in parallel and horizontal direction in a range of 2 to 30% packing ratio. Alternatively, the fillers may be arranged in parallel cross. Gas and liquid are introduced through the inlets 3 and 4, respectively. The liquid is caused to renew its surface on the rods 2 and vigorously splashed by gas flow, increasing gas-liquid contact area. At the same time, pressure loss is drastically reduced. The process is further effective in that foreign material is not blocked and gas phase material transfer coefficient is greatly enhanced. COPYRIGHT: (C)1979,JPO&Japio | ||||||
| 185 | Column for exchanging heat and mass between gas or vapor and liquid | JP8343877 | 1977-07-12 | JPS5372779A | 1978-06-28 | IWAN PIYOOTOROUITSUCHI SUROBOD |
| 186 | Kiekisukurabaashitsu | JP12842475 | 1975-10-27 | JPS5167584A | 1976-06-11 | OTSUTOO EMU SARUMIENTO; PIITAA EKUHORUMU |
| 187 | Haishutsukukinainishojirutankasuisoobunrisuruhohoto sochi | JP12976575 | 1975-10-28 | JPS5166278A | 1976-06-08 | BARUTAA BURAUN; GYUNTAA HOFUMAN |
| Apparatus for separating hydrocarbons from flue gas and the like, including a gas scrubber, a collecting container supplying the scrubber with wash oil, and a vacuum distillation container receiving wash oil discharged from the scrubber. | ||||||
| 188 | METHOD AND SYSTEM FOR ELIMINATING PARTICLES, GASES AND OR LIQUIDS FLOATING IN AIR | EP17382293.3 | 2017-05-22 | EP3406317A1 | 2018-11-28 | PÉREZ DÍAZ, José Luis |
The invention discloses a method for removing particles, gases and/or liquids from floating in air comprising the step of spraying a first fog of liquid droplets in a volume of air to be cleaned from particles, gases and/or liquids, wherein the size of the liquid droplets is between 2.5 and 20 microns. |
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| 189 | Vorrichtung und Verfahren zur Abscheidung von Staub | EP15160998.9 | 2015-03-26 | EP3072572A1 | 2016-09-28 | Esser, Ralf; Reither, Karl |
Die vorliegende Erfindung betrifft eine Vorrichtung und ein kontinuierliches Verfahren zur Abscheidung von Staub. Insbesondere betrifft die Erfindung eine Vorrichtung und ein kontinuierliches Verfahren zur energieoptimierten Abscheidung von Staub, wobei ein Differenzdruckwäscher mit einstellbaren Venturikehlen einem Differenzdruckwäscher umfassend ein oder mehrere Venturikehlen und eine oder mehrere Hybriddüsen vorgeschaltet ist. |
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| 190 | METHOD FOR SCRUBBING GAS IN A CASCADE-TYPE WET SCRUBBER AND A CASCADE SCRUBBER | EP13867107 | 2013-12-20 | EP2938421A4 | 2016-08-03 | LOUHELAINEN HARRI; KIVINEN VISA; SAARENMAA JARMO; MÄKELÄ PASI; VEHVILÄINEN JOUNI |
| 191 | METHOD FOR SCRUBBING GAS IN A CASCADE-TYPE WET SCRUBBER AND A CASCADE SCRUBBER | EP13867107.8 | 2013-12-20 | EP2938421A1 | 2015-11-04 | LOUHELAINEN, Harri; KIVINEN, Visa; SAARENMAA, Jarmo; MÄKELÄ, Pasi; VEHVILÄINEN, Jouni |
| The present invention relates to a method for scrubbing gas in a cascade-type wet scrubber. In the method gas to be cleaned and containing dust and fine impurities is led into a gas distribution chamber (13) of the cascade scrubber (10) through an inlet channel (11). From the gas distribution chamber (13) the gas is led downward through vertical cascade tubes (16) to a water tank (14) from which the purified gas is led to a droplet separator. According to the invention pressurized washing liquid is sprayed through spray nozzles (20, 21, 22) to the gas to be cleaned before and/or after said gas is discharged from the cascade tubes (16). The present invention relates also to a cascade scrubber (10). | ||||||
| 192 | A SCRUBBER SYSTEM FOR TREATING EXHAUST GAS IN A MARINE VESSEL AND METHOD OF TREATING EXHAUST GAS IN SCRUBBER SYSTEM OF A MARINE VESSEL | EP12709894.5 | 2012-02-15 | EP2678537A1 | 2014-01-01 | SUOMINEN, Ari |
| A scrubber system for treating exhaust gas in a marine vessel with a water based solution includes a first scrubber unit and a second scrubber unit, an exhaust gas inlet in the first scrubber unit and an exhaust gas outlet in the second scrubber unit and a second conduit section connecting the first scrubber unit to the second scrubber unit, a first scrubbing medium circuit and a second scrubbing medium circuit. The first scrubber medium circuit is provided with a source of scrubbing solution having a first connection to an outside of a hull of the vessel beneath the water line of the vessel and the second scrubber medium circuit is provided with a source of scrubbing solution having a source of fresh water in the vessel. | ||||||
| 193 | REINIGUNGSVORRICHTUNG ZUR REINIGUNG VON PROZESSGAS EINER REFLOWLÖTANLAGE | EP03798870.6 | 2003-09-26 | EP1551588B1 | 2013-02-27 | MEIER, Hartmut; MÜLLER, Bernd; WITTREICH, Ulrich |
| 194 | Apparatus for treating industrial waste products | EP01202397.4 | 2001-06-20 | EP1166847B1 | 2008-03-26 | Falzone, Alberto |
| The present invention refers to a water apparatus for treating industrial waste products comprising a first tank (2) containing water at a determined pressure, a second tank (4) placed inside the first tank and with which it is in communication in the lower part and which contains water at a lower pressure than that of the first tank (2), an inlet device (6, 7) of the discharge product in the second tank (4), a first dilution sector (14) of the waste product which is external to the tanks (2, 4) but in communication with the second tank (4) at one end (15) and connected to the other end with a Venturi tube (17), an outlet duct (18) of the waste product diluted by said second tank (4). The Venturi tube (17) is in communication with the first tank (2) and is suitable to create the depression of the second tank (4) with respect to the first tank (2). The second tank (4) comprises internally a further sector (10) for the dilution of the industrial waste product. |
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| 195 | WÄSCHER UND VERFAHREN ZUM REINIGEN VON GASEN | EP02761851.1 | 2002-03-05 | EP1377358B1 | 2006-06-21 | KISS, Günter, H. |
| The invention relates to a washer for purifying gases that contain particulate and/or gaseous contaminations, in which the gases are guided through an absorption column (10) onto which a washing liquid is sprayed. Additionally, a jet pump (7) operated with the washing liquid is provided which is disposed in the gas flow in series with the absorption column and generates a negative pressure in the gas flow. Preferably the jet pump is disposed in the gas flow upstream of the absorption column. The negative pressure generated in the gas flow by the jet pump should be high enough to compensate for the pressure loss in the absorption pump. | ||||||
| 196 | RAUCHGASWÄSCHER MIT EINER STÜTZKONSTRUKTION FÜR BEDÜSUNGSROHRE | EP02782701.3 | 2002-10-05 | EP1545743A1 | 2005-06-29 | WOLF, Hubert; KANKA, Helmut |
| Disclosed is a flue gas washer comprising a supporting construction (7) for spray pipes(8) used to clean at least one horizontally arranged droplet separator system. Each droplet separator system comprises droplet separator packets (15) which are mounted on carriers (2). The supporting construction (7) for the spray pipes (8) is arranged adjacent to or between the droplet separator packets (15). As a result, inspection and cleaning of the separator systems can be improved significantly. | ||||||
| 197 | Apparatus for treating industrial waste products | EP01202397.4 | 2001-06-20 | EP1166847A2 | 2002-01-02 | Falzone, Alberto |
The present invention refers to a water apparatus for treating industrial waste products comprising a first tank (2) containing water at a determined pressure, a second tank (4) placed inside the first tank and with which it is in communication in the lower part and which contains water at a lower pressure than that of the first tank (2), an inlet device (6, 7) of the discharge product in the second tank (4), a first dilution sector (14) of the waste product which is external to the tanks (2, 4) but in communication with the second tank (4) at one end (15) and connected to the other end with a Venturi tube (17), an outlet duct (18) of the waste product diluted by said second tank (4). The Venturi tube (17) is in communication with the first tank (2) and is suitable to create the depression of the second tank (4) with respect to the first tank (2). The second tank (4) comprises internally a further sector (10) for the dilution of the industrial waste product. |
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| 198 | BATCH-CONTINUOUS COUNTERCURRENT MASS EXCHANGE PROCESS | EP98954835.9 | 1998-11-04 | EP1028791A1 | 2000-08-23 | Goorden, Josephus Johannes Petrus Maria |
| Mass transfer process, in which, in at least two contact stages, and at least two liquid or gaseous phases are brought into contact with one another, at least one component being transferred between the phases and the phases moving countercurrently. The flow through at least one of the contact stages is batchwise for one phase and continuous for another phase. The phases flow through contact stages which are formed by trays in a column, which trays are opened periodically so that the phase which flows through the column in a batchwise manner flows to the next tray. | ||||||
| 199 | VENTURI SCRUBBER, SYSTEM AND METHOD | EP93916707.8 | 1993-06-22 | EP0655943B1 | 1999-09-29 | SCHWAB, James, J. |
| A venturi scrubbing system (50) optimized for removing the most optically active sized particles from a gaseous effluent stream is disclosed. Before entering the venturi the effluent stream is subcooled (20) to cause condensation of water vapor and other condensibles, thereby greatly reducing the volume of the effluent stream. In the venturi stage a scrubbing liquid is added in the form of droplets having a median diameter which optimized to remove the optically active particles. Preferably, the median diameter of the scrubbing liquid droplets is between 10 and 200 microns. A two-fluid nozzle (80) may be used to efficiently form the droplets. After passing through the scrubbing stage, which may also comprise one or more impingement plates (90), the cleansed effluent may be passed through an afterburner (100) to remove combustible materials such as organic vapors. | ||||||
| 200 | VENTURI SCRUBBER AND METHOD WITH OPTIMIZED REMOTE SPRAY | EP95938144.0 | 1995-10-02 | EP0789615A1 | 1997-08-20 | SCHWAB, James, J. |
| 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 the collection efficiency for optically active particles. The spray nozzles introduce the optimized droplets substantially upstream of the throat of the venturi such that the spray mixes with the effluent gas flow and cools the gas flow to substantially its saturation temperature prior to entering the venturi throat. This promotes collection of condensibles and inhibits the revolatilization of contaminants that are collected by the scrubbing droplets which might otherwise evaporate in the hot gas flow. The optimized droplets are highly effective in rapidly cooling the effluent gas flow. | ||||||
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