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    • 6. 发明专利
    • Control of auxiliary fuel in combustion chamber of produced gas from waste melting furnace
    • 从废物熔炼炉控制生产燃气的燃烧室中的辅助燃料
    • JPS5774514A
    • 1982-05-10
    • JP15106680
    • 1980-10-28
    • Nippon Steel Corp
    • SAKAMOTO KATSUTOSHIABE RIYUUICHIMORI KATSUHIRO
    • F23G5/24F23G5/00F23G5/50F23G7/06F23N5/02
    • PURPOSE: To economize the supply quantity of fuel by a method wherein temperature detecting terminals are provided at the front, the middle, and the rear of a combustion chamber and changes of temperatures are detected by the change of quality of the produced gas to control the supply of auxiliary fuel.
      CONSTITUTION: Temperature detecting terminals 8, 11, 12 are provided at the front, the middle, and the rear in the combustion chamber 3 of the produced gas of a melting furnace, and when the temperature lowers below the predetermined value, the auxiliary fuel control valve 9 operates to supply fuel. After a detecting temperature is restored to the predetermined value, the supply of the auxiliary fuel can be decreased gradually. In this way, calorific value of the heat generated in the combustion chamber is averaged and thermal efficiency can be maintained at a high level. Further, unburnt fuel and smoke are not generated in the combustion chamber, time period for supplying the auxiliary fuel can be shortened and the quantity of supply of the auxiliary fuel can be economized.
      COPYRIGHT: (C)1982,JPO&Japio
    • 目的:通过在燃烧室的前部,中部和后部设置温度检测端子并且通过产生的气体的质量的变化来检测温度变化的方法来节省燃料的供给量,以控制 供应辅助燃料。 构成:温度检测端子8,11,12设置在熔炉的生成气体的燃烧室3的前侧,中部和后方,当温度降低到规定值以下时,辅助燃料控制 阀9操作以供应燃料。 在检测温度恢复到预定值之后,可以逐渐减少辅助燃料的供应。 以这种方式,燃烧室中产生的热量的热值被平均化并且可以将热效率保持在高水平。 此外,在燃烧室中不产生未燃烧的燃料和烟雾,可以缩短供给辅助燃料的时间段,并且可以节省辅助燃料的供给量。
    • 7. 发明专利
    • Method for measuring solid-gas ratio in device for blowing powder and granule
    • 用于测量粉末和颗粒的装置中的固体气体比例的方法
    • JPS59182910A
    • 1984-10-17
    • JP5794183
    • 1983-04-04
    • Fuji Electric Co LtdNippon Steel Corp
    • MORI KATSUHIROKUDOU JIYUNICHINAKAJIMA YUUJITODA HIROSHIHIRAI TAKASHI
    • C21C7/00C21C5/46C21C7/072
    • C21C5/466
    • PURPOSE:To measure always exactly a solid-gas ratio by determining the change rate of the volume of the gas in a blowing tank within a prescribed time from the subtraction of the mass of only the powder and granules determined from the volume value of the blowing tank and the weighed and measured value and the flow rate of the blowing gas. CONSTITUTION:The weight WB of powder and granules B, and the sum WC of the weights WB and WA of the powder and granules A are given to calculators 11-13 in the stage of blowing the powder and granules A, B from a tank 9. The volume VG of the gas in the tank 9 is calculated by the calculators 11, 12 and 13, and is selected with a selector 14, then a correction value VG' is calculated by a calculator 15, and (Po+P)/Po is calculated from a measured pressure P and atmospheric pressure Po in a calculator 16. The change rate Qt of the volume VG' of the gas at the standard gaseous condition with time is calculated with a calculator 17. The rate Qt and the mass flow rate Qc of a carrier gas is added in an adder 18 and the weight flow rate QF of the blowing gas is calculated by multiplying the result thereof by density gammaG of the gas at the standard condition in a calculator 19. The weight flow rate QB of the blowing gas is added thereto to obtain the weight flow rate Q of the gas and a solid-gas ratio is determined from the ratio QA/Q between said flow rate and the separately calculated weight flow rate QA of the powder and granules.
    • 目的:通过从仅从粉末的体积值确定的粉末和颗粒的质量的减去的规定时间内确定吹塑罐中的气体体积的变化率来测量总体上的固体气体比例 罐和称重和测量值和吹气的流量。 构成:粉末和颗粒B的重量WB以及粉末和颗粒A的重量WB和WA的总和WC在从罐9吹入粉末和颗粒A,B的阶段中被给予计算器11-13 通过计算器11,12和13计算罐9中的气体的体积VG,并用选择器14选择,然后通过计算器15计算校正值VG',并且(Po + P)/ Po由计算器16中的测量压力P和大气压力Po计算出来。用计算器17计算标准气体条件下的气体的体积VG'的变化率Qt。速率Qt和质量流量 在加法器18中加入载气的速率Qc,通过将其结果乘以计算器19中标准状态下的气体的浓度γG来计算吹送气体的重量流量QF。重量流量QB 向其中加入吹入气体以获得气体和溶胶的重量流量Q d-气体比由所述流量与粉末和颗粒的单独计算的重量流量QA之间的比QA / Q确定。
    • 10. 发明专利
    • Air controlling method of combustion chamber for gas generated from melting furnace of solid waste
    • 用于固体废物熔融炉产生气体的燃烧室的空气控制方法
    • JPS5767719A
    • 1982-04-24
    • JP14337480
    • 1980-10-14
    • Nippon Steel Corp
    • ABE RIYUUICHISAKAMOTO KATSUTOSHIMORI KATSUHIRO
    • F23G5/50F23G5/00F23N5/00F23N5/02
    • PURPOSE: To perform the combustion with optimum air fuel ratio and keep the combustion temperature at the set temperature by a method wherein the amount of combustion air is controlled in accordance with the variance of the grade and flow rate of the fuel gas generated from solid waste melting furnace.
      CONSTITUTION: Temperature detecting terminals 7, 9 and 10 are provided at the front, middle and rear parts of the combustion chamber 3 for the gas generated from the melting furnace of solid waste such as refuse or the like. When the temperature of the detecting terminal at the front part lowers below the set temperature due to the drop of the calorific value of the generated gas, the amount of air is quickly lowered so as to have the lower limit value determined from the values of air fuel ratio μ of about 0.3W1.5, which are applied to the gas with smaller calorific value, as its lowermost amount. On the contrary, when the temperature of the detecting terminal at the front part exceeds the set temperature due to the rise of the calorific value of the generated gas, the amount of air is slowly increased so as to have the upper limit value detemined from the values of air fuel ratio μ of about 0.8W2.0, which are applied to the gas with larger calorific value, as its uppermost amount. And yet the lower limit value of secondary combustion air is set so as to have the air fuel ratio μ in respect to the total combustion air of 1.1 or more, providing against the sudden rise of the calorific value of the generated gas after the throttling down of the amount of air due to the drop of the calorific value of the generated gas to the lower limit value.
      COPYRIGHT: (C)1982,JPO&Japio
    • 目的:以最佳空燃比进行燃烧,并通过一种方法将燃烧温度保持在设定温度,其中根据固体废物产生的燃料气体的等级和流量的变化来控制燃烧空气的量 熔炉 构成:温度检测端子7,9和10设置在燃烧室3的前部,中部和后部,用于由垃圾等固体废物的熔化炉产生的气体。 当由于所产生的气体的发热量下降而使前端的检测端子的温度降低到低于设定温度时,空气量迅速降低,以便根据空气的值确定下限值 燃料比μ为约0.3-1.5,其作为其最低量被施加到具有较小热值的气体。 相反,当由于所产生的气体的发热量的上升而在前部的检测端子的温度超过设定温度时,空气量缓慢增加,从而具有从 作为其最高量,应用于具有较高热值的气体的空气燃料比率μ为约0.8-2.0的值。 然而,二次燃烧空气的下限值被设定为使得相对于总燃烧空气的空气燃料比mu为1.1以上,以防止在节流之后产生的气体的发热量的突然上升 由于所产生的气体的发热量下降而导致的空气量下降到下限值。