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    • 1. 发明专利
    • Exhausted gas-treating device
    • 排气处理装置
    • JP2007245074A
    • 2007-09-27
    • JP2006074779
    • 2006-03-17
    • Mitsubishi Heavy Ind Ltd三菱重工業株式会社
    • OKADA KENICHIOKINO SUSUMUHONJO SHINTAROKAMIYAMA NAOYUKINAKAMURA TSUMORUTAKEUCHI YASUHIRONAKAYAMA YOSHIO
    • B01D53/50B01D53/77B03C3/013
    • PROBLEM TO BE SOLVED: To provide an exhausted gas-treating device which efficiently collects SO
      3 in an exhausted gas without reducing the treatment efficiency of a flue-gas desulfurization device, the gas-treating device being simple in composition and restraining an increase in device cost.
      SOLUTION: The exhausted gas-treating device, which has an electrical dust precipitator between an exhausted gas source and a flue-gas desulfurization device, is provided with an exhausted gas temperature-lowering means which lowers a temperature of an exhausted gas until SO
      3 in the exhausted gas becomes a SO
      3 fume, the temperature-lowering means being provided on either the inlet side or outlet side of the electrical dust precipitator. In addition, a charging and adsorbing means is provided on the inlet side of the flue-gas desulfurization device to making charged solid particles adsorb the SO
      3 fume from the exhausted gas temperature-lowering means. By this, the solid particles in which the SO
      3 fume is adsorbed are fed into the flue-gas desulfurization device to remove the SO
      3 .
      COPYRIGHT: (C)2007,JPO&INPIT
    • 要解决的问题:为了提供一种在排气中有效收集SO 3 SB 3的排气处理装置,而不降低烟道气脱硫装置的处理效率,气体处理装置 组成简单,限制了设备成本的增加。 解决方案:在排气气体源和烟道气脱硫装置之间具有电除尘器的排气处理装置设置有排气降温装置,其降低排气的温度直到 排气中的SO 3 SB <3> 成为SO 3 SB 3,降温装置设置在电除尘器的入口侧或出口侧。 此外,在烟道气脱硫装置的入口侧设置充填吸附装置,使得带电固体颗粒从排气降温装置吸附SO 3 SB 3。 由此,吸附有SO 3 SB 3的固体颗粒被送入烟道气脱硫装置以除去SO 3 SB 3。 版权所有(C)2007,JPO&INPIT
    • 2. 发明专利
    • Air cleaning apparatus
    • 空气净化装置
    • JP2006150208A
    • 2006-06-15
    • JP2004343468
    • 2004-11-29
    • Mitsubishi Heavy Ind Ltd三菱重工業株式会社
    • SUZUMURA HIROSHIHANEDA MICHIONAKAMURA TSUMORUFUJIMOTO HITOSHI
    • B01D53/56B01D53/18B01D53/50B01D53/77
    • Y02A50/2345
    • PROBLEM TO BE SOLVED: To provide an air cleaning apparatus realizing simple regeneration of an absorbent while suppressing splash of liquid having washed the absorbent. SOLUTION: The air cleaning apparatus 10 comprises a duct 11; an electrostatic precipitator 12; an absorber 13 disposed downstream from the electrostatic precipitator 12 in the duct 11 in the air 1 passing direction, and having the porous absorbent carrying an absorbing component absorbing and removing nitrogen dioxide in the air 1; spray nozzles 14 spraying an aqueous solution 2 of the absorbing component onto the absorbent of the absorber 13 and a feed pump 15, etc.; a shutter 16 provided at an air 1 inlet port side of the absorber 13 and adjusting opening of an inlet port of the absorber 13; a liquid reservoir 11a provided between the electrostatic precipitator 12 and the absorber 13 in the duct 11; and a jet nozzle 17 blowing out the aqueous solution 2 remaining in the absorber 13 from the inlet port of the absorber 13 and an air blower 18, etc. COPYRIGHT: (C)2006,JPO&NCIPI
    • 要解决的问题:提供一种空气净化装置,其实现吸收剂的简单再生,同时抑制洗涤了吸收剂的液体飞溅。 解决方案:空气净化装置10包括管道11; 静电除尘器12; 在空气1通过方向上设置在管道11中的静电除尘器12的下游的吸收体13,具有吸收空气1中的二氧化氮吸收吸收成分的多孔质吸收体的吸收体13; 将吸收组分的水溶液2喷射到吸收器13的吸收剂上的喷嘴14和进料泵15等; 设置在吸收器13的空气1入口侧的吸气口16和吸收器13的入口的调节开口; 设置在导管11内的静电除尘器12和吸收体13之间的液体储存器11a; 以及喷射嘴17,从吸收体13的吸入口吹送残留在吸收体13中的水溶液2和送风机18等。(C)2006,JPO&NCIPI
    • 8. 发明专利
    • PRODUCTION OF POTABLE WATER
    • JPS61167495A
    • 1986-07-29
    • JP839485
    • 1985-01-22
    • MITSUBISHI HEAVY IND LTD
    • UGAWA NAOHIKONAKAMURA TSUMORUKONDO MASAMI
    • C02F1/68C02F1/66
    • PURPOSE:To eliminate entirely the need for an alkaline agent which is hereto fore required or to require just a small amt. thereof even when said agent is necessary by passing a gas contg. no carbon dioxide into fresh water after passage through a filter consisting of limestone, etc., to maintain the pH of said fresh water at a prescribed value. CONSTITUTION:This method produces potable water by blowing the gas contg. the carbon dioxide generated form a desalting device 1 for sea water by an evaporation method to the fresh water formed by said device 1 in a CO2 absorption column 2 to form the carbonic acid-contg. water then passing the water through the filter 3 packed with the granular limestone and/or dolomite. The gas contg. no carbon dioxide is passed from a blower 5 to the fresh water in a water storage tank 4 after the passage through the filter 3 to maintain the pH of the fresh water in the tank 4 at the prescribed value in the above- mentioned method. The need for the alkaline agent which is heretofore required for pH adjustment is eliminated entirely or the amt. thereof to be used is considerably decreased, by which the running cost is considerably reduced.
    • 9. 发明专利
    • Classification and collection of fine particle
    • 细颗粒的分类和收集
    • JPS61120651A
    • 1986-06-07
    • JP24181184
    • 1984-11-16
    • Mitsubishi Heavy Ind Ltd
    • HAMADA TAKAYOSHINAKAMURA TSUMORU
    • B03C7/02
    • PURPOSE: To enable the classification of fine particles with a particle size of up to about several μm W 0.01μm, by changing the intensity of the electric field in a classifier corresponding to the particle size of fine particles to be classified.
      CONSTITUTION: Solid-gas mixed phase gas containing fine particles and purified sheath air are introduced into a classifier 3 from inlet nozzles 10, 12 and high voltage is applied to a discharge wire 7 and a collection plate 8 to generate corona discharge. Fine particles in the classifier 3 are charged negatively by corona discharge and moved to the plus side of the collection plate 8 and moved vertically by sheath air flowing along the surface of the collection plate 8 in an air curtain form and, therefore, finally moved to the vector direction of the vertical moving speed of sheath air and the horizontal moving speed by corona charge. As a result, when a necessary particle size is classified, by applying a certain constant electric field in the classifier 3, only fine particles to be classified are guided to the collector from an opening part 4.
      COPYRIGHT: (C)1986,JPO&Japio
    • 目的:通过改变分级机中对应于待分级细颗粒的粒径的电场强度,使颗粒尺寸高达约几μm〜0.01μm的微粒分类。 构成:将来自含有细颗粒和净化的护套空气的固体气体混合气体从入口喷嘴10,12引入分级器3,并将高电压施加到放电线7和收集板8以产生​​电晕放电。 分选机3中的细颗粒通过电晕放电带负电,并移动到收集板8的正面,并以气帘形式沿着收集板8的表面流动的护套空气垂直移动,因此最终移动到 护套空气的垂直移动速度的矢量方向和电晕电荷的水平移动速度。 结果,当必要的粒径被分类时,通过在分级器3中施加一定的恒定电场,只有待分类的细颗粒从开口部分4被引导到集电器。
    • 10. 发明专利
    • Method for making drinking water from fresh water
    • 从新鲜水生产饮用水的方法
    • JPS61114792A
    • 1986-06-02
    • JP23488284
    • 1984-11-09
    • Mitsubishi Heavy Ind Ltd
    • NAKAMURA TSUMORUUGAWA NAOHIKOYAMAUCHI YOSHIKI
    • C02F1/68C02F1/66
    • C02F1/66
    • PURPOSE:To make it possible to achieve miniaturization, by providing a flow passage for supplying fresh water to a carbon dioxide absorbing tower and a bypass pipe for supplying fresh water to a filter so as to bypass the absorbing tower. CONSTITUTION:The flow amount of fresh water in a line 1 is measured by a fresh water flow amount measuring terminal 9 and the control of the flow amount in a bypass flow passage C is performed on the basis of the measured value. Next, the total concn. of carbonic acid at the inlet of a filter 4 is controlled by a detection terminal 5 and the flow amount of the carbon dioxide- containing gas supplied to a carbon dioxide absorbing tower 3 by a regulation valve 11. The flow amount ratio of the supply line (g) of fresh water to the carbon dioxide absorbing tower 3 and the bypass line C of the absorbing tower 3 is regulated by a fresh water flow amount regulation valve 8 to increase the setting range of the total concn. of carbonic acid in carbon dioxide- containing water at the inlet of the filter 4. If the proper flow amount ratio of fresh water is selected, the carbon dioxide absorbing tower 3 can be made compact.
    • 目的:为了实现小型化,可以通过设置向二氧化碳吸收塔供给淡水的流路和向过滤器供给淡水以旁路吸收塔的旁通管。 构成:通过淡水流量测量端子9测量管线1中的淡水的流量,并且基于测量值进行旁路流路C中的流量的控制。 接下来, 的过滤器4的入口处的碳酸由检测端子5和通过调节阀11供给到二氧化碳吸收塔3的含二氧化碳的气体的流量进行控制。供给管路的流量比 (g)到吸收塔3的二氧化碳吸收塔3和旁通管线C的淡水由淡水流量调节阀8调节,以增加总浓度的设定范围。 的碳酸在过滤器4的入口处的含二氧化碳的水中。如果选择适当的淡水量,可以使二氧化碳吸收塔3紧凑。