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    • 1. 发明专利
    • Control method of oxygen concentration in combustion exhaust gas
    • 燃烧排气中氧浓度的控制方法
    • JPS61110809A
    • 1986-05-29
    • JP22885484
    • 1984-11-01
    • Ebara Corp
    • MIURA IKUOFURUKAWA MASAAKI
    • F23G5/50F23N5/00F23N5/18
    • F23N5/006F23N5/18F23N2025/04F23N2037/02F23N2041/18
    • PURPOSE:To permit to restore an appropriate air-fuel ratio within shorter time for the rapid increase of the combustion volume in the incinerator by a method wherein a differential value with respect to time for an internal pressure in the incinerator is seeked for, by which the basic operating volume is revised and composed, and based on that data the operating panel for adjusting air volume is operated. CONSTITUTION:PV01, an output concerning the furnace internal pressure sent from a furnace internal pressure transmitter 15, is sent to a differential computing element 21, to which a differential computing is made, and its differential value is transformed into signal y2, which is allowed to be sent to an adder 23 only for the case that the furnace internal pressure is varied to the positive side. In the adder 23, MV12, an output operating signal computed from an oxygen concentration contained in the combustion exhaust, and the said signal y2 are composed, which enable to actuate SV03, the setting value of the secondary air adjusting gage 26, variable. A flow rate of the secondary combustion air 8 is detected by a flow detector 24, which is compared with the setting value SV03 by the operating signal MV03, that is able to actuate a damper 10 to control the secondary air flow rate. In this controlling process, the setting value SV03 is made variable by the signal MO02 from the adder 23, and the cascade control is applied to the secondary air flow rate.
    • 目的:允许在更短的时间内恢复适当的空燃比,以便焚化炉中的燃烧体积迅速增加,其中相对于焚烧炉内部压力的时间的差值被寻求,由此, 基本操作量进行修改和组合,并根据该数据操作调节风量的操作面板。 构成:将来自炉内压变送器15的炉内部压力的输出PV01发送到差分运算元件21,并进行微分运算,将其差分值变换为信号y2,允许 只有在炉内压力变化到正侧的情况下才被送到加法器23。 在加法器23中,MV12根据燃烧排气中包含的氧浓度计算的输出运算信号和所述信号y2,能够使SV03动作,二次空气调节量规26的设定值是可变的。 二次燃烧空气8的流量由流量检测器24检测,流量检测器24通过操作信号MV03与设定值SV03进行比较,能够致动阻尼器10以控制二次空气流量。 在该控制处理中,通过来自加法器23的信号MO02使设定值SV03变化,并对二次风量进行级联控制。
    • 2. 发明专利
    • Method of furnace pressure control
    • 炉压控制方法
    • JPS6149929A
    • 1986-03-12
    • JP17160284
    • 1984-08-20
    • Ebara Corp
    • MIURA IKUOFURUKAWA MASAAKI
    • F23G5/50F23N3/00F23N5/00
    • F23N3/002F23N2023/36F23N2025/02F23N2025/04F23N2033/02F23N2035/04F23N2035/06F23N2041/18
    • PURPOSE:To surely prevent the furnace pressure from becoming a positive pressure in an incinerator of urban rubbish etc. by determining whether the detected furnace pressure is higher or lower than the set value, and, when the detected value is higher than the set value, making the gain of the control system larger than that gain which is obtained when the detected value is lower than the set value. CONSTITUTION:The furnace pressure of an incinerator 1 becomes the output PV1 via a pressure transmitter 10 and a primary delay filter 15. By a subtracting unit 16, the difference from the set value SV of a PID adjusting unit 11 is determined. By an input compensation nonlinear arithmetic unit 17, when SV PV1 is selected to output PV3. In response to the output PV3, the PID computation is conducted in the PID adjusting unit 11 to output MV1, and the output MV0 is outputted via an adding unit 20. As the actuating output MV0 has become larger when SV PV1, the actuating speed of the damper 4 is made higher by the output MV0, the furnace pressure is promptly prevented from being increased to become a positive pressure.
    • 目的:通过确定检测到的炉压是否高于或低于设定值,确保炉膛压力在城市垃圾焚烧炉等中成为正压,并且当检测值高于设定值时, 使得控制系统的增益大于当检测值低于设定值时获得的增益。 构成:焚烧炉1的炉压通过压力传感器10和主延迟滤波器15成为输出PV1。通过减法单元16,确定与PID调节单元11的设定值SV的差。 通过输入补偿非线性运算单元17,当SV PV1时获得的增益大于输出PV3。 响应于输出PV3,在PID调节单元11中进行PID运算以输出MV1,并且通过加法单元20输​​出输出MV0。当SV SV时,致动输出MV0变大 PV1,通过输出MV0使阻尼器4的致动速度更高,立即防止炉压升高成正压。
    • 3. 发明专利
    • Method for preventing seizure of membrane falling type concentration boiler
    • 用于防止薄膜型浓缩锅炉碰撞的方法
    • JPS59169502A
    • 1984-09-25
    • JP4078183
    • 1983-03-14
    • Ebara Corp
    • KAMIYA ICHIROUHAYASHI YOSHISHIGEMIURA IKUO
    • B01D1/22C02F1/08
    • PURPOSE: To prevent the seizure of a concn. boiler and to enhance working efficiency by enlarging the tolerant limit operation range of a concn. apparatus, in performing the operation of a membrane falling type concn. boiler, by controlling the inflow amount of the raw solution from an inlet by a relatively simple control method.
      CONSTITUTION: In order to prevent the seizure in a membrane falling type concn. boiler 11 by controlling the flow amount of a raw solution at the inlet of said boiler 11, at first, the concn. D
      0 of the concn. solution in the outlet pipe 13 of the concn. boiler 11 and the evaporation amount G
      0 in a vapor pipe 15 are detected. The flow amount of the concn. solution per the unit peripheral length of the heat transfer surface in the concn. boiler 11 is calculated by operating said detected values by an operator 18 and subjected to the comparison operation with the solution amount of the conc. solution per a predetermined unit peripheral length required in preventing the seizure and output y
      1 for determining the min. necessary inlet flow amount F
      1 of the raw solution is operated on the basis of the operated values. On the other hand, output MV for determining the flow amount F
      1 required in holding the concn. D
      0 of the outlet conc. solution to a predetermined value is operated and the outputs y
      1 MV are subjected to comparison operation in an operator 19 to output a value for increasing F
      1 as y
      2 while the set value of the inlet flow amount of the raw solution is controlled by y
      2 and the inlet flow amount F
      1 of the raw solution is controlled by the controlled set value.
      COPYRIGHT: (C)1984,JPO&Japio
    • 目的:防止扣押 锅炉,并通过扩大公司的容限限制运行范围来提高工作效率。 在进行膜下降式运行时的装置。 通过相对简单的控制方法控制来自入口的原料溶液的流入量。 构成:为了防止坠落类型中的癫痫发作。 通过控制在锅炉11的入口处的原料溶液的流量,首先, 浓浓的D0 浓缩液出口管13中的溶液。 锅炉11和蒸气管15中的蒸发量G0被检测。 浓度的流量 解决方案每个单元的周长长度的传热表面的浓度。 锅炉11由操作者18通过操作所述检测值进行计算,并进行比较运算。 解决方案,每个预定的单位外围长度,以防止发作和输出y1确定最小。 基于操作值操作原始溶液的必要入口流量F1。 另一方面,用于确定保持浓度所需的流量F1的输出MV。 出口浓度D0 操作预定值的解决方案,并且在操作器19中对输出y1 MV进行比较操作,以将原始溶液的入口流量的设定值控制为y2,并将F1增加的值输出为y2,并将入口 原始溶液的流量F1由受控设定值控制。
    • 5. 发明专利
    • Control method of solution concentrating boiler
    • 浓缩锅炉的控制方法
    • JPS59169501A
    • 1984-09-25
    • JP4078083
    • 1983-03-14
    • Ebara Corp
    • KAMIYA ICHIROUHAYASHI YOSHISHIGEMIURA IKUO
    • B01D1/00C02F1/04
    • PURPOSE: To make it possible to control the concn. of a conc. solution in an extremely stable state, by automatically and continuously compensating the P.I.D. set value of a concn. controller regardless of the change in coefficient of process gain while holding said set value to an initial set value.
      CONSTITUTION: A raw solution concn. D
      1 , a raw solution flow amount F
      1 , a conc. solution concn. D
      0 and an evaporation amount G
      0 are detected from the raw solution pipe 12, a concn. pipe 13 and a steam pipe 15 of a concn. boiler by detectors 1W4 and the deviation Z of the concn. D
      0 and a set value is outputted by a concn. controller 17 and an operator 18 issues output (y) on the basis of the transmission function Y
      0 operated from the aforementioned detected values and the deviation Z while output MV is operated in the controller 17 by P.I.D. operation based on P.I.D. constant and a raw solution flow amount set value and flow amount F
      1 are compared by a flow amount controller 16 to operate a valve 5. In addition, process gain coefficient K
      p is operated on the basis of the aforementioned detected values by the operator 18 and α is set to fixed coefficient to select the function Y
      0 =α/K
      p . By this method, the extremely stable automatic operation of the concn. control of the concn. solution is enabled.
      COPYRIGHT: (C)1984,JPO&Japio
    • 目的:使得可以控制浓度 的浓度 解决方案处于非常稳定的状态,通过自动和连续补偿P.I.D. 设定一个浓度值 控制器,而不管过程增益系数的变化,同时将所述设定值保持在初始设定值。 规定:原始解决方案 D1,原始溶液流量F1,浓度 解决方案 D0,蒸发量G0从原料溶液管12检测出。 管13和一个蒸汽管15。 锅炉由检测器1-4和浓度的偏差Z组成。 D0,设定值由浓度输出。 控制器17和操作器18基于从上述检测值操作的传动功能Y0和偏差Z发出输出(y),同时通过P.I.D在控制器17中操作输出MV。 基于P.I.D. 常数和原始溶液流量设定值和流量F1通过流量控制器16进行比较,以操作阀5.此外,基于操作者18的上述检测值操作处理增益系数Kp,并且α 被设置为固定系数以选择函数Y0 =α/ Kp。 通过这种方法,极大的稳定的自动操作 控制浓度 解决方案已启用。