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    • 5. 发明专利
    • Operation of incinerator
    • 焚化炉的操作
    • JPS61114007A
    • 1986-05-31
    • JP23591384
    • 1984-11-08
    • Ebara Corp
    • FURUKAWA MASAAKI
    • F23G5/50F23N1/00
    • F23N1/002F23N2021/10F23N2041/18
    • PURPOSE:To improve a function by a method wherein a feed rate of dust supplying to an incinerator is controlled and the proper amount of evaporation is reset when a deviation is generated between the amount of the average dust treatment at a given time during an optional period and the amount of the standard dust treatment. CONSTITUTION:The proper amount of evaporation is obtained from the amount of the standard dust treatment and the heat release value of the dust and is set to a control meter 17, then, it is compared with the amount of the proper evaporation by measuring of the amount of evaporation in boiler 20. According to this method, the feed rate of the dust supplying to the incinerator is controlled, and the deviation generated between the amount of the dust treatment at the passage point of the given time during the optional period and the amount of the dust treatment estimated based on the amount of standard dust treatment is computed by a comparison operator 25c. When the deviation thereof is larger than a predetermined value, the amount of average dust treatment at the remaining 8 hours is obtained again from the expected dust residue and the actual amount of the dust remaining in a dust pit 2, thereafter, the value thereof may be reset as the amount of standard dust treatment.
    • 目的:通过一种方法来改善功能,其中控制焚烧炉供应的粉尘的进料速率并且在任意时间段内在给定时间内的平均粉尘处理量之间产生偏差时重置适当的蒸发量 和标准粉尘处理量。 构成:从标准粉尘处理量和粉尘的放热值得到适当的蒸发量,并设置在控制仪表17上,然后将其与适当蒸发量进行比较 锅炉20中的蒸发量。根据该方法,控制供给到焚化炉的粉尘的供给速度,并且在任意时间段内在给定时间的通过点处的粉尘处理量与 通过比较运算器25c计算基于标准粉尘处理量的灰尘处理量。 当其偏差大于预定值时,从预期的粉尘残留物和剩余在粉尘坑2中的实际尘埃量再次获得剩余8小时的平均粉尘处理量,此后其值可以 复位为标准粉尘处理量。
    • 6. 发明专利
    • Fluidized-bed type combustion furnace
    • 流化床型燃烧炉
    • JPS59195019A
    • 1984-11-06
    • JP6924083
    • 1983-04-21
    • Ebara Corp
    • MURAMATSU HIROSHIFURUKAWA MASAAKI
    • F23C10/00F23G5/50F23N1/02F23N5/00F23N5/18
    • F23N5/006F23N1/022F23N5/18F23N2037/16F23N2037/18
    • PURPOSE:To prevent production of NOX, by a method wherein the air fed to a fluidized-bed combustion furnace is divided into a primary air and a secondary air. CONSTITUTION:A furnace is provided with a first flow meter 12 for measuring the flow rate of a primary air, a second flow meter 14 for measuring the flow rate of a secondary air, an oxygen concentration meter 16 for measuring oxygen concentration in exhaust gas, and a computing part 17 which, based on output signals from the flow meters 12 and 14, and the oxygen concentration meter 16, computes an xygen concentration condition on a fludizied bed surface 18. A first regulating part 19 outputs a control signal which regulates the flow rate of a primary air, based on a deviation between an oxygen concentration condition outputted from the computing part 17 and a previously set oxygen concentration condition on the fluidized bed surface 18. A second regulating part 20 outputs a control signal which controls the flow rate of a secondary air so that an output signal from the oxygen concentration meter 16 attains a previously set value. This prevents production of NOX.
    • 目的:为了防止生产NOX,通过将进料到流化床燃烧炉的空气分成一次空气和二次空气的方法。 构成:炉具有用于测量一次空气流量的第一流量计12,用于测量二次空气流量的第二流量计14,用于测量废气中氧浓度的氧浓度计16, 以及基于来自流量计12和14的输出信号和氧浓度计16的计算部分17计算浊化床表面18上的xygen浓度条件。第一调节部分19输出控制信号, 基于从计算部17输出的氧浓度条件与流化床表面18上预先设定的氧浓度条件之间的偏差,一次空气的流量。第二调节部20输出控制流量 使得来自氧浓度计16的输出信号达到预先设定的值。 这样可以防止生产NOX。
    • 7. 发明专利
    • METHOD FOR CONTROLLING FURNACE PRESSURE
    • JPH11325437A
    • 1999-11-26
    • JP7804799
    • 1999-03-23
    • EBARA CORP
    • FURUKAWA MASAAKI
    • F23G5/50
    • PROBLEM TO BE SOLVED: To adjust the rate of combustion air to slow fluidization and completely suppress the rise in furnace pressure, by arranging an adjusting damper in a fluidizing air line for feeding the combustion air from the lower part of a fluidized bed in a fluidized bed incinerator or a gasification furnace for incinerating or gasifying urban garbage and the like. SOLUTION: Into an incinerator 1 are supplied a raw material 7, combustion air 8-1 and a secondary combustion air 8-2 respectively. In this case, a bypass line BL is installed in a fluidizing air line of the combustion air 8-1, and an adjusting damper 81 of furnace pressure is arranged therein. The combustion air 8-1 is blown into the upper part of the incinerator 1, and the blowing amount is adjusted by the adjusting damper 81. The furnace pressure is detected by a detection end 9 provided on the upper part of the incinerator 1, the detection output is inputted into an operator 61 by means of a transmitter 10, the operation output is inputted into the adjusting damper 81 to control the furnace pressure. As a result, in the case the furnace pressure is increased, the fluidizing amount of the combustion air is restricted to slow fluidization.
    • 8. 发明专利
    • JPH05296430A
    • 1993-11-09
    • JP11843292
    • 1992-04-13
    • EBARA CORP
    • OCHI YUJISATO KEIICHIFURUKAWA MASAAKIISHIKAWA RYUICHI
    • F23G5/50
    • PURPOSE:To provide a method and a device for operating a fluidized bed combustion device in which a flowing of excessive secondary air into a combustion chamber is closed when fuel is fully diminished and a surging of a blower can be prevented. CONSTITUTION:In a fluidized bed combustion device for igniting raw material of which quality and amount are varied, means 18 and 19 for sensing a lack of raw material are installed within the combustion furnace and a secondary air supplying system 14 is provided with a secondary air blower 19 and a secondary air flowing adjusting damper 10 for preventing flowing-in of the secondary air when a lack of raw material is detected. Then, a secondary air circulating line 15 through the secondary air blower 19 is provided or a secondary air bypassing line 16 for flowing secondary air into a discharged gas passage 17 at a downstream side of the combustion chamber is provided. When the lack of raw material is detected, the secondary air flowing adjusting damper 10 is closed and operation can be carried out for passing the secondary air to the line 15 or 16, and further the forced air supplying system 11 can be provided with a forced air bypassing line 12 for flowing a part of the forced air into the discharging gas passage 17 at the downstream side of the combustion chamber.
    • 9. 发明专利
    • COMBUSTION CONTROL IN FLUIDIZED BED FURNACE
    • JPH0375406A
    • 1991-03-29
    • JP21282389
    • 1989-08-18
    • EBARA CORP
    • NAITO TAKEYUKIKURODA YOSHIKIFURUKAWA MASAAKIYOSHIDA YUTAKA
    • F23N5/00F23C10/28F23G5/50
    • PURPOSE:To maintain substantially constant the state of combustion regardless of the variation in the charge to be incinerated that is charged into a furnace by changing the volume of air that is sent into a furnace from below its fluidized bed so as to maintain the temperature of the fluidized bed in a specified range of temperature by the output of furnace bed temperature detection means. CONSTITUTION:A calculator 11 carries out the calculation Y1 to calculate a fluidizing air volume setting value, SV1 from its brightness signal PV0. A calculator 12 carries out the calculation Y2 to calculate a fluidizing air volume setting value, SV2 from its fluidizing air volume setting value SV1 and furnace bed temperature detection signal PV1 of a furnace bed temperature detection end 6, and outputs the calculation result to a flow rate control regulator 13. A flow rate control regulator 13 outputs control signal MV to control a bypass control valve 3 to a bypass control valve 3 from a fluidizing air volume setting value SV2 and a fluidizing air detection signal PV3 for the fluidizing air volume that is sent into a fluidized layer 4 from a fluidizing air detection end 7, and controls the volume of air that bypasses to the free board 2 and controls the volume of the fluidizing air that is sent into the fluidized layer 4. With this arrangement the combustion quantity can be maintained substantially constant regardless of a change in the charge to be incinerated that is charged into the furnace.
    • 10. 发明专利
    • BOILER DRUM PRESSURE CONTROL METHOD
    • JPH01312303A
    • 1989-12-18
    • JP14261088
    • 1988-06-09
    • EBARA CORP
    • FURUKAWA MASAAKI
    • F22B35/00F22B1/18F23G5/50
    • PURPOSE:To control the pressure of a boiler drum without the generation of visible smoke and nitrogen oxide by selecting a control system whose output is smaller out of two control systems based on the application of a low selector and operating a dust collector. CONSTITUTION:Generally, there is only available a pressure control system which controls the quantity of dust based on the pressure of a boiler, directly manipulating a dust collector. However, the characteristic difference between the pressure of a boiler and the concentration of combustion waste gas oxygen will induce the generation of visible smoke in the shortage of oxygen. To solve this problem, attempts are made to cascade set a predetermined value of a forced air flow rate controller 18 based on an operation output MV01 and a reference value, compare it with a setting value V06 of a hearth oxygen concentration controller 21 through arithmetic operations and thereby obtain an operation output MV06. A low selector 28 selects a lower output out of the two operation outputs MV01 and MV06 and obtains an operation output Y04. This construction makes it possible to maintain the pressure of a boiler drum within a specified range and the concentration of waste gas oxygen within a proper range as well based on the control of the quantity of dust collection.