会员体验
专利管家(专利管理)
工作空间(专利管理)
风险监控(情报监控)
数据分析(专利分析)
侵权分析(诉讼无效)
联系我们
交流群
官方交流:
QQ群: 891211   
微信请扫码    >>>
现在联系顾问~
热词
    • 1. 发明专利
    • Ash melting device
    • ASH熔融设备
    • JP2006003010A
    • 2006-01-05
    • JP2004179814
    • 2004-06-17
    • Babcock Hitachi Kkバブコック日立株式会社
    • TANIGUCHI YUKIHISAFUJIWARA NAOKIYAMAMOTO MANABUKOBAYASHI KAZUKIISHII SHUHEI
    • F23J1/00B09B3/00C04B5/00F23J1/02F23J1/06F27D15/02
    • PROBLEM TO BE SOLVED: To provide an ash melting device capable of inexpensively and easily obtaining slag of high strength and high quality.
      SOLUTION: This ash melting device comprises an ash melting furnace 10 for burning and melting the ash (a) to obtain molten slag (b), and a water tank 15 mounted at a lower part of a molten slag dropping port 10B of the ash melting furnace 10 for granulating the molten slag (b) by water and recovering the same, and a slag receiver 16 is mounted on an intermediate part of a connection body 14 for connecting the ash melting furnace 10 and the water tank 15. The molten slag (b) from the molten slag dropping port 10B is received by the slag receiver 16, cooled to a specific temperature, and temporarily kept at the specific temperature. A hammer 17 is oscillatably mounted on an upper part of the slag receiver 16 to crush the slag (b) on the slag receiver 16.
      COPYRIGHT: (C)2006,JPO&NCIPI
    • 待解决的问题:提供能够廉价且容易地获得高强度和高质量的炉渣的灰熔融装置。 解决方案:该灰熔融装置包括用于燃烧和熔化灰分(a)以获得熔融炉渣(b)的灰熔炉10和安装在熔渣落下口10B的下部的水箱15 用于通过水造粒熔融炉渣(b)并回收炉渣的灰熔化炉10,并且在用于连接灰熔化炉10和水箱15的连接体14的中间部分上安装有渣块16。 来自熔渣落渣口10B的熔渣(b)被渣接收器16接收,冷却至特定温度,暂时保持在特定温度。 锤17可摆动地安装在炉渣接收器16的上部,以将炉渣(b)粉碎在炉渣接收器16上。版权所有(C)2006,JPO&NCIPI
    • 2. 发明专利
    • Gasifying melting furnace
    • 加热熔炼炉
    • JP2002372212A
    • 2002-12-26
    • JP2001179144
    • 2001-06-13
    • Babcock Hitachi Kkバブコック日立株式会社
    • FUJIWARA NAOKIMARUMOTO TAKAHIROSENJU TORU
    • F23G5/027B09B3/00F23G5/00F23G5/16
    • Y02E50/30
    • PROBLEM TO BE SOLVED: To provide a gasifying melting furnace wherein the rate of operation of the melting furnace and reliability of the same are improved and the running cost is reduced by eliminating turbulence factors against a flow in a melting furnace and against a slag rate due to cooling air in a stating burner for the melting furnace. SOLUTION: The gasifying melting furnace comprises a gasifying combustion furnace for combusting refuse, a melting furnace for completely combusting thermal decomposition gas including ash and char particles produced in the gasifying combustion furnace, and a thermal decomposition gas flue. A combustion chamber communicated to the foregoing melting furnace through the flue is provided together with provision of an oil spray nozzle and a starting burner in the combustion chamber, and the flue is joined with the thermal decomposition gas flue, and further hot air produced owing to combustion in the combustion chamber is blown into the melting furnace through the thermal decomposition gas flue.
    • 要解决的问题:提供一种气化熔炉,其中通过消除熔化炉中的流动的湍流因素和与炉渣速率相关的炉渣速率,提高了熔炉的操作速度及其可靠性,并降低了运行成本 以在用于熔化炉的定位燃烧器中冷却空气。 解决方案:气化熔炉包括用于燃烧垃圾的气化燃烧炉,用于完全燃烧包括在气化燃烧炉中产生的灰分和焦炭颗粒的热分解气体的熔化炉和热分解气体烟道。 在燃烧室中设置有连接到上述熔化炉的燃烧室,同时在燃烧室中设置喷油嘴和起始燃烧器,并且烟道与热分解气体烟道接合,并且由于 燃烧室内的燃烧通过热分解气体烟道吹入熔化炉。
    • 9. 发明专利
    • PRODUCTION OF FUNCTIONAL BAG FILTER MATERIAL
    • JPH11244636A
    • 1999-09-14
    • JP5196698
    • 1998-03-04
    • BABCOCK HITACHI KK
    • KOBAYASHI KAZUKIYAMAMOTO MANABUFUJIWARA NAOKI
    • B01D39/14B01D46/02B01D53/94
    • PROBLEM TO BE SOLVED: To maintain the activity of a functional bag filter for a long time and to prevent the active material from dropping during operation, to be splashed on the downstream side and released to the outside of the system, by previously depositing active fine particles on a base cloth and laminating the both faces of the base cloth with a filter material. SOLUTION: The base cloth 2 released from a base cloth roll 1 is carried by a roller 3a and impregnated with a catalyst slurry 4 in a catalyst slurry tank 5 filled with the catalyst slurry 4. Then the cloth is carried by a roller 3e and dried by a heater 6 to form a catalyst-carrying cloth 15, which is introduced into a filter material depositing device 7. In the filter material depositing device 7, a filter material 8 is supplied to both faces of the catalyst carrying cloth 15. After the catalyst carrying cloth 15 is held between a roller 3f and a roller 3g with a filter material holding sheet 9 inserted, the filter material 8 is pressed and deposited to both surfaces of the catalyst carrying cloth 15 by a press-depositing device 10. The obtd. material is wound up as a functional bag filter material 11 on a functional bag filter material roll 12.
    • 10. 发明专利
    • FLY ASH TREATING DEVICE AND FLY ASH TREATMENT
    • JPH1190390A
    • 1999-04-06
    • JP26204297
    • 1997-09-26
    • BABCOCK HITACHI KK
    • MATSUDA TOSHIAKIFUJIWARA NAOKIYAMAMOTO MANABUOKU TSUNEO
    • B09B3/00
    • PROBLEM TO BE SOLVED: To provide a fly ash treating device which is compact and easy in maintenance and by which metallic elements contained in a waste gas from an ash melting furnace are separated and recovered with high efficiency and to provide a fly ash treating method. SOLUTION: This fly ash treating device is composed of a fly ash treating machine 2, a recovery device 4, a circulating blower 5, a temp. controller 8 and a fly ash collector 19. The fly ash collected by the collector 19 is charged into a heating chamber 2b through a hopper 2a and heated by a waste gas from an ash melting furnace 10 introduced into a duct 2c. The temp, of the heating chamber 2b is first controlled to 800-850 deg.C and kept at the temp. for several hours and further, the outlet temp. of the recovery device is controlled to 200 deg.C. Consequently, only Pb and Cd components are selectively vaporized and recovered. Subsequently, the fly ash left in the heating chamber is heated to 1000-1100 deg.C and kept at the temp. for several hours. At this time, the outlet temp. of the recovery device is maintained at 200 deg.C as well. Accordingly, Na, Cl and K components are selectively vaporized and recovered. Finally, a high-b. p. material such as Ca, Al, S remaining in the heating chamber is extracted from the bottom of the heating chamber.