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    • 4. 发明专利
    • Fluidized bed furnace with rectangular heating pipes
    • 带矩形加热管的流化床炉
    • JPS57120007A
    • 1982-07-26
    • JP506981
    • 1981-01-19
    • Babcock Hitachi Kk
    • TACHIBANA KEITAROUKAWADA SHINTAKAMI NOBUAKI
    • F28F13/00F22B1/02F22B31/00F23C10/24F23C10/28F23G5/30
    • F22B31/0023
    • PURPOSE:To improve the contact between each of the heating pipes and fluidizing medium and to raise the collection rate of heat in a fluidized bed when heat is collected in a fluidized bed through heating pipes arranged there by a method wherein groups of heating pipes of many stages are arranged so that they are intersected at right angles in the direction of the bed height of the fluidized bed. CONSTITUTION:Groups 2 of evaporating pipes are made up by arranging a plurality of evaporating pipes 2a in parallel in a fuidized bed furnace body 1 and connecting them to a header 5. A group of evaporating pipes 4 formed similarly by arranging a plurality of evaporating pipes 4a in parallel and connecting them to a header 5 is arranged so that it falls at right angles with said group 2 of evaporating pipes. On the side of the group 4 of evaporating pipes a group 6 of overheaters is arranged so that the latter is parallel to the former. In this manner, when the supply water in the groups 2, 4 of evaporating pipes is heated and reaches a drum 13 through pipes 12a, 12b before the starting of the fluidized bed is completed, the fluidizing medium is mixed and stirred well and heating efficiency is raised because each group 2, 4 of evaporating pipes are arranged at right angles with each other.
    • 目的:为了改善每个加热管和流化介质之间的接触,并且当通过加热配管在其中的管道在流化床中收集热量时,提高流化床中的热量收集率,其中一组加热管道 这些阶段被布置成使得它们在流化床的床高度的方向上以直角相交。 构成:蒸发管2组通过将多个蒸发管2a平行布置在通风床炉体1中并将其连接到集管5而构成。一组蒸发管4通过将多个蒸发管2a排列成多个蒸发管 4a并联并将其连接到集管5上,使得其与蒸发管的所述组2成直角。 在蒸发管4组的一侧,设置过热器组6,使得后者与前者平行。 以这种方式,当流化床启动之前蒸发管组2,4中的供水被加热并通过管道12a,12b到达滚筒13时,流化介质被充分搅拌和加热效率 由于蒸发管的每组2,4彼此成直角地排列,所以升高。
    • 5. 发明专利
    • METHOD OF OPERATING SWIRLING JET FLOW BED FURNACE
    • JPS5457371A
    • 1979-05-09
    • JP12350377
    • 1977-10-17
    • BABCOCK HITACHI KK
    • KAWADA SHINKAJIMOTO NOBORU
    • F23G5/50F23G5/00F23G5/30F23G7/00
    • PURPOSE:To provide a method of operating swirling jet flow bed furnace for combusting EP-ash, according to which temperature of exhaust gas at the outlet of the furnace is kept higher than the dew point of vapor of sulfuric acid contained in the exhaust gas, and the exhaust gas is cooled rapidly through detection of temperature of the subsequent exhaust gas flow, whereby it is enabled to operate the furnace in stable manner, while preventing sticking of dust to the wall of the furnace and inner surface of ducts. CONSTITUTION:EP-ash is supplied from EP-ash supplying means 8 and it is swirled forcibly together with swirling medium 10 such as sand. Combustible components in the ash are combusted and carbons contained in the ash is also combusted, so that temperature of the gas in the furnace is raised. Temperature of the combustion gas is detected by detector 12 and controlled such that it is 700-730 deg.C in the swirling jet flow bed and 650-700 deg.C at free board section 13. Combustion gas is passed through outlet 14 of the furnace and delivered into duct 15. Cooling air supplying means 16-19 are provided at the top of the furnace for cooling the combustion gas rapidly to about 500 deg.C. By the cooling the combustion gas, compounds having a low melting point, contained in combustion residue, are solidified, so that sticking of the residue to the wall of the furnace or other portions of the system can be prevented.
    • 6. 发明专利
    • Fluidized bed furnace for burning unburnt gas
    • 用于燃烧未燃气体的流化床炉
    • JPS57120009A
    • 1982-07-26
    • JP507281
    • 1981-01-19
    • Babcock Hitachi Kk
    • TACHIBANA KEITAROUKAWADA SHINTAKAMI NOBUAKI
    • F23C10/18B01J8/28F23C10/00F23C10/24F23G5/30
    • F23C10/24B01J8/28F23C10/005
    • PURPOSE:To burn fuel completely by a method wherein a small reburning fluidized bed furnace is arranged in the air chamber of a fluidized bed furnace body, ashes and unburnt fuel generated on the surface of the fluidized bed of the body is supplied to the reburning fluidized bed furnace through an extracting pipe. CONSTITUTION:In the fluidized bed furnace body 1, the fluidized bed 3 and an air chamber 4 are provided respectively above and under a porous plate 2. Now, an unburnt gas extracting pipe 5 is arranged in the middle of the fluidized bed 3, its upper end is opened on the surface part of the fluidized bed 3, its lower end penetrates through the porous plate 2 and opens in the fluidized bed 10 of a small reburning fluidized bed furnace 6 arranged in the air chamber 4. Besides, a burnt ash exhaust pipe 7 is connected to the reburning fluidized bed 6 and the other end is connected to an ash hopper 8. Thus, the ashes and the unburnt fuel which have been collected on the surface of the fluidized bed 3 are introduced into the reburning fluidized bed furnace 6 through the extracting pipe 5 and can be burnt completely in the fluidized bed 10.
    • 目的:通过在流化床炉体的空气室内设置小型再燃流化床炉的方法完全燃烧燃料,将在本体流化床表面产生的灰烬和未燃燃料供应至再燃流化床 床式炉通过提取管。 构成:在流化床炉体1中,流化床3和空气室4分别设置在多孔板2的上方和下方。现在,在流化床3的中部设置未燃气体提取管5, 上端在流化床3的表面部分开口,其下端穿过多孔板2并在布置在空气室4中的小型再沸流化床炉6的流化床10中打开。此外, 排气管7连接到再沸流化床6,另一端连接到灰斗8.因此,已经收集在流化床3的表面上的灰和未燃燃料被引入再沸流化床 炉6通过提取管5,并且可以在流化床10中完全燃烧。
    • 8. 发明专利
    • METHOD AND DEVICE FOR CONTROLLING TEMPERATURE IN MOVING LAYER
    • JPS54141073A
    • 1979-11-01
    • JP4787978
    • 1978-04-24
    • BABCOCK HITACHI KK
    • KAWADA SHINSHIMOMURA MITSUHIROUEMURA TOSHIO
    • F27B15/16F23G5/00F23G5/30F23G5/50F23G7/00F23N5/00F23N5/24F27B15/18
    • PURPOSE:To control the temperature in the layer of the moving layer incinerator by means of water cooling walls which surround the moving layer portion of the incinerator and water cooling pipes provided within the moving layer, thereby lowering the time constant of the incinerator and, hence, burning up the substance to be disposed effectively. CONSTITUTION:A porous plate 2 provided in the lower portion of a moving layer incinerator 1 is lined up by cooling water pipes and a moving layer 4 has cooling water pipes provided therein and also coiled water cooling pipes 8 mounted so that they will form a water cooling wall 9. Then, the temperature in the layer of the incinerator 1 is transmitted from a temperature emitter 10 to a regulating box 13, which sends signals for controlling the amount of the cooling water which flows through the cooling water pipes 6 inside the layer and the water cooling wall 9. The cooling water fed from a pump 14 flows, after regulated in the amount by a control valve 16, through the cooling water pipes 6 and the cooling wall 9 and then exhaused in the form of vapour. Accordingly, it is possible to lower the time constant of the incinerator 1 and thereby to burn up the substance to be disposed which contains nitrogen compounds such as EP ashes without producing any nitrogen oxides.
    • 9. 发明专利
    • SWIRLING JET FLOW BED FURNACE
    • JPS5457370A
    • 1979-05-09
    • JP12350277
    • 1977-10-17
    • BABCOCK HITACHI KK
    • KAWADA SHINKAJIMOTO NOBORU
    • F23G7/00F23G5/00F23G5/30
    • PURPOSE:To provide a swirling jet flow bed furnace for combusting EP-ash, in which height of the hollow sleeve portion of the furnace is made sufficiently high for completely carrying out combustion of ammonia and for proceeding reaction of non-reacted substances, whereby sticking of sticky substances to the wall of the furnace and inner surface of the ducts can be prevented and it is enabled to operate the furnace continuously. CONSTITUTION:In combusting EP-ash in a swirling jet flow furnace, combustion gas is made to stay long the the furnace so as to completely combust ammonia produced by decomposition of ammonium sulfate. Ammonium sulfate is decomposed into NH3 and SO3 in swirling jet flow bed 1, and NH3 is in turn decomposed into nitrogen gas and water, whereas SO3 is decomposed into SO2. Here, in order that these decomposed substances may not be re-united in the combustion gas after cooling, height of hollow sleeve portion 13 is made sufficiently high, preferably more than 5 meters, to lower the content of ammonia at the outlet of the sleeve portion 13. Further, the gas speed is designed at 0.5-1.0 m/s, preferably at 0.7 m/s, so that reaction of non-reacted substances be promoted in the sleeve portion 13.
    • 10. 发明专利
    • Fluidized furnace with height of fluidized bed being controlled
    • 具有流化床控制高度的流化炉
    • JPS57122206A
    • 1982-07-30
    • JP800681
    • 1981-01-23
    • Babcock Hitachi Kk
    • TACHIBANA KEITAROUKAWADA SHINTAKAMI NOBUAKI
    • F27B15/00F23C10/28F23C10/30F23G5/30
    • F23C10/30
    • PURPOSE:To recover the heat to utilize efficiently, from fluidized medium drained out of a furnace by controlling the height of fluidized bed, by providing an air preheating chamber in which medium drain pipes to drain fluidized medium out of a furnace are provided. CONSTITUTION:A plurality of drain pipes 2a, 2b, and 2c for draining fluid medium are respetively connected to the side wall of a body 1 of fluidized furnace, and the other ends of the pipes are connected to a medium reservoir 3. An air preheating chamber 5 is formed by shrouding the whole length of a casing 4 of the above-mentioned drain pipes 2a, 2b, and 2c, and the heat discharged from drain pipes 2a, 2b, and 2c is recovered by the air fed via a piping 15, when the fluidized medium is drained. The preheated air is fed into an air chamber 10 of a body 1 of fluidized furnace by a preheated air pipe 16 and is utilized to keep the temperature of a fluidized bed 12 high, or to heighten the temperature of the bed.
    • 目的:通过提供一个空气预热室,通过控制流化床的高度来回收热量以有效地利用从流化床排出的流化介质,其中提供了将流化介质排出炉的介质排放管。 构成:用于排出流体介质的多个排水管2a,2b和2c分别连接到流化炉主体1的侧壁,并且管的另一端连接到介质储存器3.空气预热 通过覆盖上述排水管2a,2b和2c的壳体4的整个长度来形成室5,并且通过经由管道15供给的空气回收从排水管2a,2b和2c排出的热量 当流化介质排出时。 预热的空气通过预热的空气管道16被供给到流化床主体1的空气室10中,并且用于将流化床12的温度保持在较高水平,或者提高床的温度。