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    • 2. 发明授权
    • Method of controlling combustion in fluidized bed incinerator
    • 流化床焚烧炉燃烧控制方法
    • US4986198A
    • 1991-01-22
    • US415351
    • 1989-07-28
    • Takeyuki NaitoYoshiki KurodaHiroshi Yoshida
    • Takeyuki NaitoYoshiki KurodaHiroshi Yoshida
    • F23N3/00F23C10/28F23G5/30F23G5/50F23N1/02F23N5/00F23N5/08
    • F23N1/022F23C10/28F23G5/30F23G5/50F23N5/006F23G2207/1015F23G2207/102F23G2207/103F23G2207/112F23G2207/30F23N1/02F23N2029/20F23N2035/06F23N2037/18F23N5/08
    • In a fluidized bed incinerator for burning matter to be incinerated charged into a furance by causing fluidization of a fluidizing medium with the assistance of air fed from the lower portion of a fluidized bed, a combustion control method is arranged such that: the combustion rate of matter for incineration in the furnace is detected by a combustion rate detecting means, and, when the combustion rate exceeds a predetermined level the amount of air fed from the lower portion of the fluidized bed is reduced; and, simultaneously, the amount of air blown into a space above the fluidized bed is increased so as to control and maintain the combustion rate of the matter to be burnt in the furnace at the predetermined level and to suppress fluctuations in the amount of combustion air, the amount of exhaust gas, the oxygen concentration in the exhaust gas and the amount of gas remaining unburnt or the like. The combustion control method is also applicable to a fluidized bed incinerator constructed to include a plurality of air chambers formed at the lower portion of the fluidized bed, through which chambers the air is fed into the incinerator and the combustion rate of matter for incineration is controlled by regulating the amount of air fed from the air chamber disposed at the portion where the matter charged is dropped.
    • PCT No.PCT / JP88 / 00437 Sec。 371日期:1989年7月28日 102(e)日期1989年7月28日PCT提交1988年4月30日PCT公布。 出版物WO88 / 08504 日期:1988年11月3日。在流化床焚化炉中,通过在流化床下部空气供给下引起流态化介质的流化,将要焚烧的物质燃烧,从而燃烧控制方法 使得:通过燃烧速率检测装置检测炉中焚烧物质的燃烧速率,并且当燃烧速率超过预定水平时,从流化床下部供给的空气量减少; 并且同时增加吹入流化床上方空间的空气量,从而控制并保持在炉中燃烧的物质的燃烧速率达预定水平并抑制燃烧空气量的波动 ,排气量,废气中的氧浓度和未燃烧气体的量等。 燃烧控制方法也适用于流化床焚烧炉,其构造为包括形成在流化床下部的多个气室,空气通过该室供入焚化炉,并且用于焚化的物质的燃烧速率被控制 通过调节从设置在被填充物质的部分落下的空气室供给的空气的量。
    • 3. 发明授权
    • Process for recovery of chemicals from pulping waste liquor
    • 从制浆废液中回收化学品的方法
    • US4212702A
    • 1980-07-15
    • US938076
    • 1978-08-30
    • Saburo MizuguchiIsao NomuraTakeyuki NaitoMasato OnoderaKouji Saito
    • Saburo MizuguchiIsao NomuraTakeyuki NaitoMasato OnoderaKouji Saito
    • D21C11/00D21C11/12D21C11/02
    • D21C11/122D21C11/0057Y10S423/03
    • A process for recovery of chemicals from a sodium sulfite pulping waste liquor is disclosed in which a smelt obtained from the waste liquor is introduced into an aqueous slurry containing solidified smelt while make up water and a weak aqueous slurry are supplied to effect incomplete dissolution of the smelt into the aqueous slurry to maintain the content of total solid and the temperature of the slurry at constant levels, the resulting aqueous slurry is subjected to a solid-liquid separation to obtain a wet cake having the molar ratio of S/Na.sub.2 O substantially equal to that of the smelt, the wet cake is mixed with hot particles of sodium carbonate and sodium sulfite while hot air is supplied to effect oxidation of sodium sulfide in the wet cake to sodium sulfite and then the oxidized product is dissolved in aqueous medium and sulfur dioxide-containing gas, preferably the exhaust gas from the recovery boiler, is contacted with the resulting aqueous solution to convert sodium carbonate into sodium sulfite, whereby the overall process is carried out in a closed system and the sulfur component and the sodium component present in the waste cooking liquor are recovered and regenerated into a cooking liquor.
    • 公开了从亚硫酸钠制浆废液中回收化学品的方法,其中从废液中获得的熔体被引入含有固化的熔融物的含水浆料中,同时补充水,并且提供弱的含水浆料以实现不完全溶解 熔化到含水浆料中以将总固体含量和浆料的温度保持在恒定水平,将所得含水浆料进行固液分离,得到S / Na 2 O摩尔比基本上等于 在熔融的情况下,将湿饼与热碳酸钠和亚硫酸钠混合,同时供给热空气,使湿滤饼中的硫化钠氧化成亚硫酸钠,然后将氧化产物溶于含水介质和二氧化硫 的气体,优选来自回收锅炉的废气与所得水溶液接触以将碳酸钠转化成 至亚硫酸钠,由此整个过程在封闭系统中进行,并且回收废弃蒸煮液中存在的硫成分和钠成分并再生成蒸煮液。
    • 4. 发明授权
    • Process for recovery of chemicals from pulping waste liquor
    • 从制浆废液中回收化学品的方法
    • US4141785A
    • 1979-02-27
    • US778551
    • 1977-03-17
    • Saburo MizuguchiIsao NomuraTakeyuki NaitoMasato OnoderaKouji Saito
    • Saburo MizuguchiIsao NomuraTakeyuki NaitoMasato OnoderaKouji Saito
    • D21C11/00D21C11/12D21C11/02
    • D21C11/122D21C11/0057Y10S423/03
    • A process for recovery of chemicals from a sodium sulfite pulping waste liquor is disclosed in which a smelt obtained from the waste liquor is introduced into an aqueous slurry containing solidified smelt while make up water and a weak aqueous slurry are supplied to effect incomplete dissolution of the smelt into the aqueous slurry to maintain the content of total solid and the temperature of the slurry at constant levels, the resulting aqueous slurry is subjected to a solid-liquid separation to obtain a wet cake having the molar ratio of S/Na.sub.2 O substantially equal to that of the smelt, the wet cake is mixed with hot particles of sodium carbonate and sodium sulfite while hot air is supplied to effect oxidation of sodium sulfide in the wet cake to sodium sulfite and then the oxidized product is dissolved in aqueous medium and sulfur dioxide-containing gas, preferably the exhaust gas from the recovery boiler, is contacted with the resulting aqueous solution to convert sodium carbonate into sodium sulfite, whereby the overall process is carried out in a closed system and the sulfur component and the sodium component present in the waste cooking liquor are recovered and regenerated into a cooking liquor.
    • 公开了从亚硫酸钠制浆废液中回收化学品的方法,其中从废液中获得的熔体被引入含有固化的熔融物的含水浆料中,同时补充水,并且提供弱的含水浆料以实现不完全溶解 熔化到含水浆料中以将总固体含量和浆料的温度保持在恒定水平,将所得含水浆料进行固液分离,得到S / Na 2 O摩尔比基本上等于 在熔融的情况下,将湿饼与热碳酸钠和亚硫酸钠混合,同时供给热空气,使湿滤饼中的硫化钠氧化成亚硫酸钠,然后将氧化产物溶于含水介质和二氧化硫 的气体,优选来自回收锅炉的废气与所得水溶液接触以将碳酸钠转化成 至亚硫酸钠,由此整个过程在封闭系统中进行,并且回收废弃蒸煮液中存在的硫成分和钠成分并再生成蒸煮液。
    • 5. 发明授权
    • Fluidized bed combustion furnace
    • 流化床燃烧炉
    • US5178531A
    • 1993-01-12
    • US741514
    • 1991-08-08
    • Takeyuki NaitoKeiichi SatoHiroshi Yoshida
    • Takeyuki NaitoKeiichi SatoHiroshi Yoshida
    • F23C10/00F23G5/30
    • F23C10/002F23C10/00F23G5/30
    • A fluidized bed combustion furnace comprising a throttle section (12) formed directly above a fluidized bed (18) so that the flow velocity of combustion gas in the throttle section becomes higher than the terminal velocity of grains or particles of a fluidizing medium which have a mean diameter, secondary air supply ports (22) provided in the throttle section in a plurality of stages, a free board section (13) formed above the throttle section, the free board section having such a cross-sectional area that the gas flow velocity becomes lower than the terminal velocity of mean diameter grains or particles of the fluidizing medium, two or more combustion gas inlets (16a) and (17a) of combustion gas passages (16) and (17) provided in an area of the ceiling portion of the free board section which is not coincident with the plane of projection of the throttle section, and a junction chamber (25) provided at the outlets of the combustion gas passages so that high-temperature gases passing through the combustion gas passages collide and merge with each other in the junction chamber.
    • PCT No.PCT / JP90 / 00187 Sec。 371日期1991年8月8日 102(e)日期1991年8月8日PCT提交1990年2月16日PCT公布。 第WO90 / 09549号公报 日本1990年8月23日。一种流化床燃烧炉,包括直接形成在流化床(18)上方的节流部分(12),使得节流部分中的燃烧气体的流速变得高于颗粒或颗粒的末端速度 具有平均直径的流化介质,设置在所述节流部分中的多个级的二次空气供给口(22),形成在所述节流部分上方的自由板部分(13),所述自由板部分具有这样的横截面, 气体流速变得低于流化介质的平均直径颗粒或颗粒的末端速度的截面积,设置在燃烧气体通道(16)和(17)中的两个或更多个燃烧气体入口(16a)和(17a) 所述自由板部的顶部与所述节流部的突起面不一致的区域,以及设置在所述燃烧气体通路的出口处的接合室(25),使得高温 通过燃烧气体通道的气体在接合室中相互碰撞并相互合并。