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    • 5. 发明专利
    • Thermal decomposition method for carbonaceous raw material
    • 碳分解原料的热分解方法
    • JP2008150477A
    • 2008-07-03
    • JP2006339093
    • 2006-12-15
    • Kyoto UnivNippon Steel Corp国立大学法人京都大学新日本製鐵株式会社
    • HASHIMOTO SHIGERUNAGAI KAZUNORIMAE KAZUHIROHASEGAWA ISAOOMUKAI YOSHIKAGEKATOU YASUHIKO
    • C10B49/06B09B3/00
    • Y02E50/30Y02P20/143
    • PROBLEM TO BE SOLVED: To provide a thermal decomposition method for a carbonaceous resource capable of increasing a generated combustible gas by reducing tar by utilizing a characteristic of a shaft type thermal decomposition furnace. SOLUTION: In the thermal decomposition method for the carbonaceous raw material using a move bed shaft type thermal decomposition furnace, after the carbonaceous resource charged from an upper part of the furnace and descending the inside of the furnace is thermally decomposed by a heating gas charged from a lower part of the furnace and ascending the inside of the furnace, a generated solid carbonized material is discharged from the bottom of the furnace and the generated gas and tar are discharged from an upper part of the furnace. The amount of generated tar is reduced by making a ratio of sensible heat of the charged heating gas relative to an amount of the charged carbonaceous resource to 800 Mcal/ton-1,500 Mcal/ton. COPYRIGHT: (C)2008,JPO&INPIT
    • 要解决的问题:提供一种通过利用轴式热分解炉的特征,通过降低焦油来提高产生的可燃气体的碳质材料的热分解方法。 解决方案:在使用移动床式热分解炉的碳质原料的热分解方法中,从炉上部装载并下降到炉内部的碳质物质通过加热热分解 从炉下部装入并从炉内升起的气体,产生的固体碳化材料从炉底排出,产生的气体和焦油从炉的上部排出。 通过使充电的加热气体的显热比相对于带电的碳质材料的量的比例为800Malal / ton-1500Mcal /吨来降低产生的焦油的量。 版权所有(C)2008,JPO&INPIT
    • 6. 发明专利
    • Method of treating converter by-produced gas
    • 转化器生产气体的处理方法
    • JP2006315926A
    • 2006-11-24
    • JP2005142003
    • 2005-05-16
    • Nippon Steel Corp新日本製鐵株式会社
    • EBA ATSUSHIYAMASHITA KOSUKENAGAI KAZUNORI
    • C01B32/40B01D53/14
    • Y02C10/06
    • PROBLEM TO BE SOLVED: To provide a method of treating a converter by-product gas (LDG) by which CO 2 in the LDG is reformed to CO to increase the calories of LDG and to amplify and increase the volume of the LDG. SOLUTION: In the method of treating the converter by-product gas, CO 2 contained in the by-product gas produced in a converter is removed by a CO 2 absorbing liquid supplied to an absorber and CO 2 released by regenerating the CO 2 absorbing liquid in a regeneration tower is mixed with oxygen to be blown into the converter and reacts with C in a hot metal in the converter to reform to CO. COPYRIGHT: (C)2007,JPO&INPIT
    • 要解决的问题:提供一种处理LDG中的CO 2 的转化器副产物气体(LDG)的方法,其将COG改性为CO以增加LDG的热量并放大 并增加LDG的数量。 解决方案:在处理转化器副产物气体的方法中,转化器中产生的副产物气体中所含的CO 2 通过CO 2 向吸收器供给的吸收液体和在再生塔中再生CO 2 SB吸收液释放的CO 2 与氧气混合,吹入转化器并与C反应 转换器中的一种热金属转化为CO。版权所有:(C)2007,JPO&INPIT
    • 7. 发明专利
    • Method for control of oxygen concentration and temperature of exhaust gas from rotary hearth reducing furnace
    • 控制氧化还原炉氧气浓度和排气温度的方法
    • JP2005300068A
    • 2005-10-27
    • JP2004118918
    • 2004-04-14
    • Nippon Steel Corp新日本製鐵株式会社
    • NISHIMURA TETSUYANAGAI KAZUNORI
    • C22B5/10C21B13/10F27B9/02F27B9/16F27D7/06F27D17/00
    • PROBLEM TO BE SOLVED: To enable stable reduction treatment in a rotary hearth furnace which prevents a reducing atmosphere from reacting with atmospheric air entering an exhaust duct to cause unnecessary heat generation and pressure increase, by controlling the temperature and oxygen concentration of exhaust gas without sacrificing a reduction treatment degree and the temperature and oxygen concentration of the reducing atmosphere.
      SOLUTION: Secondary combustion air is sprayed into a furnace chamber (a) just upstream of exhaust with respect to a gas flow to bring the oxygen concentration 28 of exhaust gas to a predetermined oxygen concentration, and second combustion air is next sprayed into a furnace chamber (b) upstream of the furnace chamber a to bring the temperature 29 of the exhaust gas into a predetermined temperature range. The two means are repeated until the oxygen concentration 28 and temperature 29 in the exhaust gas duct fall within the predetermined ranges. For further improved controllability, temperature control measures the furnace temperatures of the furnace chambers (a) and (b) and changes fuel and primary combustion air to bring each furnace chamber to a predetermined temperature.
      COPYRIGHT: (C)2006,JPO&NCIPI
    • 要解决的问题:为了在回转炉床炉中进行稳定的还原处理,通过控制排气的温度和氧浓度,防止还原气体与进入排气管的大气进行反应,引起不必要的发热和压力增加 气体,而不牺牲还原处理度和还原气氛的温度和氧浓度。 解决方案:二次燃烧空气相对于气流喷射到排气旁边的炉室(a)中,使废气的氧浓度28达到预定的氧浓度,然后将第二燃烧空气喷入 炉室(b)在炉室a的上游,以使废​​气的温度29达到预定的温度范围。 重复这两种方式,直到排气管道中的氧浓度28和温度29落在预定范围内。 为了进一步提高可控性,温度控制测量炉室(a)和(b)的炉温,并改变燃料和初级燃烧空气,使每个炉室达到预定温度。 版权所有(C)2006,JPO&NCIPI