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    • 2. 发明专利
    • Slag discharge system and method for operating the same
    • SLAG放电系统及其操作方法
    • JP2012088000A
    • 2012-05-10
    • JP2010235948
    • 2010-10-20
    • Mitsubishi Heavy Ind Ltd三菱重工業株式会社
    • HAYATA YASUOMIYATA YASUYUKIKOYAMA TOMONORIISHII HIROMISHINADA OSAMU
    • F23J1/02
    • PROBLEM TO BE SOLVED: To provide a slag discharge system capable of easily and efficiently discharging slag, and a method for operating the same.SOLUTION: The slag discharge system includes a slag reservoir 26 for storing water granulated slag 19, a slurry tank 40 which stores the water granulated slag 19 discharged from the slag reservoir 26 and slurry liquid 29 and converts them into slag slurry 41, a slag slurry conveying part 28 having a slag slurry pump 43 for conveying the slag slurry 41, a slag storage tank 30 which separates slurry water 29 from the slag slurry 41 and stores the water granulated slag 19, a recovery pipe 62 for recovering discharge water 33 and supplying it to the slurry tank 40, a weight measuring device 201 for detecting the slag amount of the water granulated slag 19 dropped into or discharged from the slag reservoir 26, and a control means 202 for controlling driving of a slag conveyor 26b in such a manner that the slag conveyor 26b completes the discharge before the next water granulated slag supplying time, according to the amount of slag to be supplied.
    • 要解决的问题:提供能够容易且有效地排出炉渣的排渣系统及其操作方法。 排渣系统包括用于储存水粒状渣19的渣储存器26,储存从渣储存器26排出的水粒状渣19和浆液29并将其转化为渣浆41的浆料槽40, 具有用于输送炉渣浆料41的炉渣浆料泵43的渣浆输送部28,将渣浆水29与渣渣41分离并储存在水渣粒子19中的渣渣槽30,回收排出水 33并将其供给到浆料槽40中,用于检测滴入或从渣槽26排出的水粒状渣19的渣量的重量测量装置201,以及用于控制渣输送器26b的驱动的控制装置202 这样,炉渣输送器26b根据要供给的炉渣的量,在下一个造粒渣供给时间之前完成排出。 版权所有(C)2012,JPO&INPIT
    • 3. 发明专利
    • Slag discharge system
    • SLAG排放系统
    • JP2012037189A
    • 2012-02-23
    • JP2010179874
    • 2010-08-10
    • Mitsubishi Heavy Ind Ltd三菱重工業株式会社
    • MIYATA YASUYUKIHAYATA YASUOKOYAMA TOMONORI
    • F23J1/02
    • PROBLEM TO BE SOLVED: To provide a slag discharge system capable of discharging slag more easily and properly.SOLUTION: The slag discharge system includes a slag cooling section for cooling the discharged slag, a slurry tank for storing the slag discharged from the slag cooling section and liquid, a slag slurry conveying section for slurrying the slag stored in the slurry tank by the liquid and conveying it, a slag storage tank for discharging the liquid from the slag slurry conveyed from the slag slurry conveying section and storing the slag, and a recovering section for recovering the liquid discharged from the slag storage tank and supplying the same to the slurry tank.
    • 要解决的问题:提供能够更容易且适当地排出炉渣的排渣系统。 解决方案:排渣系统包括用于冷却排出的炉渣的炉渣冷却段,用于储存从炉渣冷却段和液体排出的炉渣的浆料罐,用于使储存在浆料罐中的炉渣浆料的渣浆输送段 通过液体输送,用于从从渣浆输送部输送的渣渣排出液体并储存炉渣的渣槽;以及回收部,用于回收从渣储罐排出的液体,并将其供给到 泥浆罐。 版权所有(C)2012,JPO&INPIT
    • 4. 发明专利
    • Slag discharge system
    • SLAG排放系统
    • JP2011074274A
    • 2011-04-14
    • JP2009228592
    • 2009-09-30
    • Mitsubishi Heavy Ind Ltd三菱重工業株式会社
    • KOYAMA TOMONORIYOSHIDA NAOSHIGESHINADA OSAMUHAYATA YASUO
    • C10J3/46C10J3/52F27D15/02
    • C10J3/52C10J3/506C10J3/72C10J2300/1628Y02E20/16Y02E20/18
    • PROBLEM TO BE SOLVED: To provide a slag discharge system having high degree of freedom of layouts, high reliability and enabling to stably discharge the slag at low cost. SOLUTION: This slag discharge system is equipped with a slag-slurry tank 23 for recovering slag S from a slag reservoir 21 into water to slurry it; slag-slurry piping 25 connecting the slag-slurry tank 23 and a slag storage tank 13; and a pump 27 provided to the slag-slurry pipings 25, sucking slag-slurry in the slag-slurry tank 23 and delivering it to the slag storage tank 13. The slag discharge system is so constituted that the slag S discharged from a gasification furnace 1, generating combustible gas, is quenched in cooling water to become vitrified slag S; the slag S discharged out of the system together with cooling water from the gasification furnace 1 is recovered in the slag reservoir 21; and the slag S is conveyed from the slag reservoir 21 to the slag storage tank 13. COPYRIGHT: (C)2011,JPO&INPIT
    • 要解决的问题:提供一种具有高自由度,高可靠性和能够以低成本稳定地排出炉渣的排渣系统。

      解决方案:该排渣系统配备有渣渣槽23,用于将炉渣S从渣池21回收到水中以将其浆化; 连接熔渣槽23和炉渣储罐13的渣浆管25; 以及设置在渣渣管25上的泵27,在渣浆槽23中吸取渣浆并将其输送到渣储罐13.渣排出系统构成为从气化炉排出的炉渣S 1,产生可燃气体,在冷却水中淬火成为玻璃化渣S; 与来自气化炉1的冷却水一起排出系统的炉渣S在炉渣贮存器21中回收; 并且炉渣S从炉渣贮存器21输送到炉渣储存箱13.版权所有(C)2011,JPO&INPIT

    • 5. 发明专利
    • HEAT FLUX METER
    • JPH10227703A
    • 1998-08-25
    • JP2889797
    • 1997-02-13
    • MITSUBISHI HEAVY IND LTDYAMARI SANGYO KK
    • KAI SHOICHIHAYATA YASUOKAWASHIMA HACHIROTSUJITAKE KAZUYOSHI
    • G01K17/08
    • PROBLEM TO BE SOLVED: To provide a small heat flux meter with good durability. SOLUTION: This heat flux meter includes a heat-receiving-surface tube 2 in the form of a cylinder closed at an end face and being smaller in diameter than the end face, an outer frame pipe 3 in the form of a cylinder closed at a first end and having a hole in the first end, with its bore being equal to the outside diameter of the end face of the heat receiving surface tube 2, an inner pipe 6 connected to the first end of the heat receiving surface tube 2, an outer pipe 4 connected to the first end of the outer frame pipe 3, an intermediate pipe 5 placed between the inner and outer pipes, a sheathed-pipe-type thermocouple 7a having its end inserted and secured in place by boring a hole in the center of the end face of the heat receiving surface tube 2, and a sheathed-pipe-type thermocouple 7a having its end inserted and secured in place by boring a radial hole in the side face of the heat receiving surface tube 2, the heat receiving surface tube 2 being inserted into the outer frame pipe 3, and the heat receiving surface tube 2, the outer frame pipe 3, and a sheathed pipe being made from the same material.
    • 9. 发明专利
    • COAL GASIFIER
    • JPH0625680A
    • 1994-02-01
    • JP18244692
    • 1992-07-09
    • MITSUBISHI HEAVY IND LTD
    • HAYATA YASUONAKAJIMA YOICHIRO
    • C10J3/02
    • PURPOSE:To provide a coal gasifier whereby gasification can be conducted stably at high efficiency, and the heat-up operation can be accomplished at low cost. CONSTITUTION:Simultaneously with the start of the gasification, a compressor 12 for formed gas is started to pass a char-conveying gas (formed gas) 18 through a pipe 18'. The temperature of the formed gas at the exit of the compressor 12 is as high as 300-350 deg.C. A stop valve 20 of a heat-up device is opened, and part of the char-conveying gas (formed gas) 18 is sent as a formed gas for heat-up through the route of a char recovery pipe 18' to a heat-up pipe 19 and then to a heat-up nozzle 21, injected into a discharge valve 24 provided on the bottom of a recovery hopper 9 and evaporated to scatter drain 1 accumulated on the lower part of the recovery hopper 9. Also drain (a) adhering to the inside surface of the recovery hopper 9 is allowed to evaporate. The formed gas 23 for heat-up is sent from the recovery hopper 9 to a cyclone 8 to evaporate the drain adhering to the inside surface of a pipe at the lower part of the cyclone 8, then combined with a formed gas 16 leaving the gasifier 1 and led downstream.