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    • 1. 发明专利
    • Flue gas treatment system and flue gas treatment method
    • FLUE气体处理系统和FLAS气体处理方法
    • JP2013081876A
    • 2013-05-09
    • JP2011221536
    • 2011-10-06
    • Babcock Hitachi Kkバブコック日立株式会社
    • MITSUI YOSHIAKIIMADA NORIYUKIOMINE SHIGETOKATAGAWA ATSUSHI
    • B01D53/50B01D21/01B01D21/26B01D53/14B01D53/18B01D53/64B01D53/77
    • PROBLEM TO BE SOLVED: To prevent the re-release of Hg after desulfurization by preventing the increase in the Hg concentration on the solid side in the circulation tank of a flue gas desulfurization apparatus.SOLUTION: It has been ascertained that a low-gypsum concentration underflow 44-side liquid left after a sulfur oxide absorbent solution is extracted from the absorbent solution reservoir of a desulfurizer 3 and part of the gypsum is separated and removed by means of a first solid/liquid separator 38 is recycled as makeup water for the desulfurizer 3, the overflow 43-side liquid from the first solid/liquid separator 38 contains a high concentration of small-particle-diameter Hg. Accordingly, the underflow 44-side liquid obtained by passing the underflow 44-side liquid through a filter 40 for solid/liquid separation and the overflow 43-side liquid are combined together in a circulating water tank 41 to form recirculation water, and a coagulant is added to the recirculation water to effect the coagulation and particle size growth of high-Hg concentration fine particles recirculated into the desulfurizer 3 to thereby make it possible to efficiently perform solid/liquid separation in an absorbent solution solid/liquid separator 54 located downstream of the position of coagulant addition.
    • 要解决的问题:通过防止烟道气脱硫装置的循环罐中的固体侧的Hg浓度的增加来防止脱硫后的Hg的再释放。 解决方案:已经确定,在脱硫剂3的吸收剂溶液储存器中提取硫氧化物吸收剂溶液后残留的低石膏浓度的44侧液体,并且部分石膏通过 再循环第一固/液分离器38作为脱硫器3的补给水,来自第一固/液分离器38的溢流43侧液体含有高浓度的小粒径Hg。 因此,通过将底流44侧液体通过用于固液分离的过滤器40和溢流43侧液体而得到的底流44侧液体在循环水箱41中结合在一起,形成再循环水,凝结剂 被添加到再循环水中以实现再循环到脱硫器3中的高Hg浓度细颗粒的凝结和粒度生长,从而可以在位于下游的吸收剂溶液固/液分离器54中有效地进行固/液分离 凝结剂的添加位置。 版权所有(C)2013,JPO&INPIT
    • 2. 发明专利
    • Exhaust gas treatment apparatus of oxygen combustion system
    • 氧气燃烧系统的排气处理装置
    • JP2011110480A
    • 2011-06-09
    • JP2009267914
    • 2009-11-25
    • Babcock Hitachi Kkバブコック日立株式会社
    • MITSUI YOSHIAKIYOSHIZAKO HIDEHISAIMADA NORIYUKIODA NAOKI
    • B01D53/50B01D53/56B01D53/62B01D53/77B01D53/81F23J15/00
    • F23L7/007B01D53/343B01D53/346B01D53/504B01D53/508B01D53/56B01D53/62B01D53/75B01D2251/304B01D2251/306B01D2251/404B01D2251/606B01D2257/302B01D2257/404B01D2257/504F23C9/003F23J15/006F23J15/06F23J15/08F23J2215/20F23J2215/50F23J2217/10F23J2217/50F23J2219/20F23J2219/70Y02E20/326Y02E20/344Y02E20/346Y02E20/348Y02E20/363
    • PROBLEM TO BE SOLVED: To prevent the piping of an exhaust gas circulation section from being corroded and to prevent the fluidity and combustibility of pulverized coal inside piping of a mill from being lowered. SOLUTION: In the exhaust gas treatment apparatus equipped with an exhaust gas treatment section consisting of a coal-fueled oxygen combustion boiler 1, a denitrification apparatus 3, an air preheater 4, a dust collector 5, a desulfurization apparatus 6, and a carbon dioxide recovery apparatus 8 arranged in the given order from the upstream side of an exhaust gas duct 1 of the oxygen combustion boiler 1 to its downstream side and an exhaust gas circulation section that branches from an exhaust gas duct of the exit of the dust collector 5 or from the exit of the denitrification apparatus 6, preheats the exhaust gas by means of the air preheater 4, and returns the preheated exhaust gas to the oxygen combustion boiler 1, a heat recovery heat exchanger 13 that brings the gas temperature at the dust collector 5 entry to a temperature not more than the acid dew point of SO 3 and not less than the dew point of water is provided between the air preheater 4 and the dust collector 5, and a reheating heat exchanger 14 that brings the gas temperature to the acid dew point of SO 3 or higher is provided in the vicinity of the branched part of the exhaust gas circulation. The bringing of the gas temperature at the exit of the dust collector 5 to the acid dew point of SO 3 or lower condenses SO 3 to enable the condensed SO 3 to be removed at the dust collector 5. COPYRIGHT: (C)2011,JPO&INPIT
    • 要解决的问题:为了防止废气循环段的管道被腐蚀,并且防止磨机管道内的粉煤的流动性和可燃性降低。 解决方案:在配备有由燃煤氧化锅炉1,脱氮装置3,空气预热器4,集尘器5,脱硫装置6构成的废气处理部的废气处理装置中, 从氧气燃烧锅炉1的排气管道1的上游侧向其下游侧以给定的顺序配置的二氧化碳回收装置8,以及从灰尘出口的排气管道分支的排气循环部 集尘器5或脱氮装置6的出口,通过空气预热器4对排气进行预热,并将预热的废气返回到氧燃烧锅炉1,使热回收热交换器13将气体温度设定在 集尘器5在空气预热器4和集尘器5之间设置为不低于SO 3 的酸露点且不低于露点的温度, 在废气循环的分支部附近设置有使气体温度达到SO 3 SB 3以上的酸露点的再热换热器14。 使集尘器5的出口处的气体温度达到SO 3 SB 3的酸露点或更低的浓度使SO 3 冷凝,使得SO 3 SB 在除尘器5上被清除。版权所有(C)2011,JPO&INPIT
    • 3. 发明专利
    • Wet two step flue gas desulfurization apparatus and operation method of wet two step flue gas desulfurization apparatus
    • 湿式两步骤气体脱硫装置和湿法两步骤气体脱硫装置的操作方法
    • JP2009240908A
    • 2009-10-22
    • JP2008090023
    • 2008-03-31
    • Babcock Hitachi Kkバブコック日立株式会社
    • SHIMODAIRA WAKAKOMITSUI YOSHIAKIIMADA NORIYUKIMORIMOTO NOBUO
    • B01D53/50B01D47/10B01D53/18B01D53/64B01D53/68B01D53/77
    • PROBLEM TO BE SOLVED: To provide a wet two step flue gas desulfurization apparatus maintaining high performance of removing/absorbing dust or trace constituents in exhaust gas and preventing increase of a mist scattering amount scattered to a desulfurization/absorption tower at a rear flow side of a Venturi scrubber during low load operation of a boiler. SOLUTION: The wet two step flue gas desulfurization apparatus is made to have the Venturi scrubber 1 having a throat part 5 for absorbing, removing, and collecting the dust in the exhaust gas and a mist eliminator 8 for removing mist containing the dust collected by the throat part 5 at the upper stream side of the exhaust gas passage of the desulfurization/absorption tower 2 for absorbing the sulfur oxide in the exhaust gas discharged from a combustion device. A plurality of the Venturi scrubbers 1 are installed in parallel and the number of the Venturi scrubbers 1 for introducing the exhaust gas is reduced when the operation load of the combustion device is decreased than that under predetermined load. Since the plurality of the Venturi scrubbers 1 are installed in parallel and the number of them is reduced under low load, the high gas flow speed at the throat part 5 is maintained even under low load and high performance of removing/absorbing the dust is maintained. COPYRIGHT: (C)2010,JPO&INPIT
    • 要解决的问题:提供一种保持高效除尘/吸收排气中的灰尘或微量成分的湿二步烟气脱硫装置,防止散发到后部的脱硫/吸收塔的雾散射量的增加 文丘里洗涤器的流动侧在锅炉的低负荷运行期间。 解决方案:湿式两步烟气脱硫装置制成文丘里洗涤器1具有用于吸收,除去和收集废气中的灰尘的喉部5,以及用于除去含有灰尘的雾气的除雾器8 由脱硫/吸收塔2的排气通道的上游侧的喉部5收集,用于吸收从燃烧装置排出的废气中的硫氧化物。 当多个文氏管洗涤器1并联安装时,当燃烧装置的操作负载比预定负载下的操作负荷降低时,用于引入废气的文丘里洗涤器1的数量减少。 由于多个文丘里洗涤器1平行安装并且在低负载下数量减少,所以即使在低负载下也能保持喉部5处的高气体流速,并且保持除尘/吸收灰尘的高性能 。 版权所有(C)2010,JPO&INPIT
    • 4. 发明专利
    • Fuel cell power generating system
    • 燃油电池发电系统
    • JP2006310109A
    • 2006-11-09
    • JP2005131743
    • 2005-04-28
    • Babcock Hitachi Kkバブコック日立株式会社
    • OSHIMA MASAKIYATABE HIROSHIKOYAMA KAZUHITOIMADA NORIYUKIMIYATA TERUFUMI
    • H01M8/04H01M8/06H01M8/10
    • Y02E60/521
    • PROBLEM TO BE SOLVED: To appropriately cancel abnormality, corresponding to an abnormal cause by properly determining the abnormal cause of a fuel cell power generation system.
      SOLUTION: If voltage reduction of a fuel cell is voltage reduction of the cell (S3) as a whole, when a physical quantity correlated to an anode gas flow rate is less than a set value (S4), the voltage reduction of the fuel cell is determined to be caused by the lack of the amount of hydrogen (S5), when the physical quantity correlated to the anode gas flow rate is larger than the set value (S4); and when the anode gas temperature is lower than the set value, it is determined to be caused by the lack of humidification of reformed gas (S8, S9), when the anode gas temperature is higher than the set value, it is determined to be caused by CO poisoning (S8, S12). In any of the cases, the load current of the fuel cell is reduced (S6-S13) and a command for increasing the amount of hydrogen of the reformed gas corresponding to each cause (S7), a command for raising the anode gas temperature (S11) or a command for reducing the CO concentration of the reformed gas (S14) is outputted.
      COPYRIGHT: (C)2007,JPO&INPIT
    • 要解决的问题:通过适当地确定燃料电池发电系统的异常原因,适当地消除对应于异常原因的异常。 解决方案:如果燃料电池的电压降低是整体电池的电压降低(S3),则当与阳极气体流量相关的物理量小于设定值(S4)时,电压降低 当与阳极气体流量相关的物理量大于设定值(S4)时,确定燃料电池由于缺少氢气而导致(S5)。 并且当阳极气体温度低于设定值时,判定为由于重整气体的加湿不足而导致(S8,S9),当阳极气体温度高于设定值时,判定为 由中毒引起(S8,S12)。 在任何情况下,燃料电池的负载电流减少(S6-S13)和用于增加与各种原因对应的重整气体的氢量的指令(S7),提高阳极气体温度的指令( S11)或用于降低重整气体的CO浓度的指令(S14)。 版权所有(C)2007,JPO&INPIT
    • 5. 发明专利
    • Operation method of hydrogen manufacturing device
    • 氢气制造装置的运行方法
    • JP2006306665A
    • 2006-11-09
    • JP2005132125
    • 2005-04-28
    • Babcock Hitachi Kkバブコック日立株式会社
    • TAKEDA YUTAKAIMADA NORIYUKIKOYAMA KAZUHITOYATABE HIROSHIARIMITSU YASUYUKI
    • C01B3/38C01B3/48H01M8/06H01M8/10
    • Y02E60/521
    • PROBLEM TO BE SOLVED: To shorten the time required for reaching ≤10 ppm CO concentration in a reformed gas of a hydrogen manufacturing device for a fuel cell. SOLUTION: The device includes a reforming reactor for forming a reformed gas containing hydrogen, a CO shift reactor for allowing carbon monoxide (CO) contained in the reformed gas to react with steam and a CO selective oxidizer for reducing a CO concentration of the reformed gas by using a gas containing oxygen as an oxidizing agent, and the device is constituted so as to supply the reformed gas passed through the CO selective oxidizer to the fuel cell. When the device is operated, the supply of the oxidizing agent to the CO selective oxidizer is stopped at least one time while supplying the reformed gas to the CO selective oxidizer, and the reduction of a CO selective oxidation catalyst of the CO selective oxidizer is performed by the hydrogen contained in the reformed gas. COPYRIGHT: (C)2007,JPO&INPIT
    • 要解决的问题:为了缩短在燃料电池用氢制造装置的重整气体中达到≤10ppmCO浓度所需的时间。 解决方案:该装置包括用于形成含氢气的重整气体的重整反应器,用于使重整气体中包含的一氧化碳(CO)与蒸汽反应的CO转化反应器和用于降低CO浓度的CO选择性氧化剂 通过使用含氧气体作为氧化剂的重整气体,该装置构成为将通过CO选择性氧化剂的重整气体供给到燃料电池。 当装置运行时,向CO选择性氧化剂供应氧化剂至少停留一次,同时向CO选择性氧化剂供应重整气体,并且执行CO选择性氧化剂的CO选择氧化催化剂的还原 通过重整气体中所含的氢。 版权所有(C)2007,JPO&INPIT
    • 9. 发明专利
    • Exhaust gas desulfurizer and oxygen combustion apparatus and method having the same
    • 排气除氧器和氧气燃烧装置及其相关方法
    • JP2011230047A
    • 2011-11-17
    • JP2010101919
    • 2010-04-27
    • Babcock Hitachi Kkバブコック日立株式会社
    • MITSUI YOSHIAKIIMADA NORIYUKIISHIZAKA HIROSHIODA NAOKI
    • B01D53/50B01D53/18B01D53/62B01D53/77F23C9/08F23L7/00
    • Y02E20/344
    • PROBLEM TO BE SOLVED: To provide an exhaust gas desulfurizer of high exhaust gas desulfurization efficiency that performs the exhaust gas treatment of different desulfurization efficiency according to an SOconcentration required for a boiler side (recirculation line side) and a COrecovery apparatus side with one desulfurizer without using a large amount of desulfurization absorption liquids, and prevents the corrosion of the COrecovery apparatus and prevents SOcondensation as the whole combustion system, and to provide an oxygen combustion system including the exhaust gas desulfurizer.SOLUTION: Oxygen combustion where fuel such as coal is combusted by a boiler using oxygen obtained by separating a nitrogen component from air is performed. An ascending current region 29 where exhaust gas flows upward and a descending current region 30 where exhaust gas flows downward are disposed in the desulfurizer 3. A recirculation outlet duct 2' for discharging a part of exhaust gas passing through a first absorption section to the outside is disposed in a space disposed in an upper part of the ascending current region 29. Exhaust gas is supplied to the boiler from the recirculation outlet duct 2' via an exhaust gas recirculation line 18, and the other exhaust gas is discharged to the COrecovery apparatus 17 for recovering COfrom the outlet duct 2.
    • 解决的问题:提供一种高排气脱硫效率的废气脱硫器,其根据所需的SO 2 浓度进行不同脱硫效率的废气处理 锅炉侧(再循环管路侧)和CO 2 回收装置侧,不使用大量的脱硫吸收液体,并且防止CO 2 恢复装置,并且防止作为整个燃烧系统的SO 2 冷凝,并且提供包括废气脱硫器的氧气燃烧系统。 解决方案:进行氧气燃烧,其中燃料如煤由使用通过从空气中分离出氮成分获得的氧气的锅炉燃烧。 排气向上流动的上升电流区域29和废气向下流动的下行电流区域30设置在脱硫器3中。一个用于将通过第一吸收部分的废气的一部分排出到外部的再循环出口管道2' 设置在设置在上升电流区域29的上部的空间中。废气通过废气再循环管线18从再循环出口管道2'供应到锅炉,而另一个废气被排放到CO 2, SB POS =“POST”> 2 恢复装置17,用于从出口管道2恢复CO 2 。版权所有(C)2012,JPO&INPIT
    • 10. 发明专利
    • Oxygen combustion type exhaust gas treatment apparatus and operation method for the same
    • 氧气燃烧类型排气处理装置及其操作方法
    • JP2011120981A
    • 2011-06-23
    • JP2009279419
    • 2009-12-09
    • Babcock Hitachi Kkバブコック日立株式会社
    • IMADA NORIYUKISHIMODAIRA WAKAKOODA NAOKI
    • B01D53/64B01D53/50B01D53/56B01D53/62F23C9/08F23J15/00F23L7/00
    • Y02E20/326
    • PROBLEM TO BE SOLVED: To provide an exhaust gas treatment apparatus which can remove mercury more surely and efficiently, although its structure is simple, in an oxygen combustion type coal-fired boiler plant, and an operation method for the exhaust gas treatment apparatus. SOLUTION: In the exhaust gas treatment apparatus, an oxygen combustion boiler 1, a denitration device 2, a heat exchanger 3, a dust collector 4, a desulfurization device 5, and a CO 2 recovery device 6 are installed in this order from the upstream side of an exhaust gas passage, and an exhaust gas circulation line 8 for subjecting exhaust gas of the outlet of the dust collector 4 or the outlet of the desulfurization device 5 to heat exchange with exhaust gas of the outlet of the denitration device 2 by the heat exchanger 3 and returning the exhaust gas to the inlet of the boiler 1 is installed and provided with a halogen supply device 23 in the exhaust gas circulation line 8. By installing the halogen supply device 23 in the exhaust gas circulation line 8 whose exhaust gas temperature is lower than the exhaust gas temperature in the vicinity of a furnace of the boiler 1, the halogen supply device 23 can be simply structured, and a supplied halogen compound can be efficiently distributed into the exhaust gas, thereby surely removing mercury. COPYRIGHT: (C)2011,JPO&INPIT
    • 要解决的问题:为了提供一种排气处理装置,虽然其结构简单,但是在氧燃烧式燃煤锅炉设备中,能够更加可靠,高效地除去汞,以及废气处理的运转方法 仪器。 解决方案:在排气处理装置中,氧燃烧锅炉1,脱硝装置2,热交换器3,集尘器4,脱硫装置5和CO 2 回收 设备6从排气通道的上游侧依次安装,并且用于使集尘器4的出口或脱硫装置5的出口的排气与废气进行热交换的废气循环管线8 通过热交换器3将废气返回到锅炉1的入口,并且在废气循环管线8中设置有卤素供给装置23.通过安装卤素供给装置23 在排气温度低于锅炉1炉附近排气温度的废气循环管线8中,能够简单地构成卤素供给装置23,能够有效地提供供给的卤素化合物 分配到废气中,从而可靠地去除汞。 版权所有(C)2011,JPO&INPIT